Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ModelicaTest_3.2.1_ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.conf.json
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaTest 3.2.1+maint.om/package.mo", uses=false)
Using package ModelicaTest with version 3.2.1 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaTest 3.2.1+maint.om/package.mo)
Using package Modelica with version 3.2.3 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo)
Using package Complex with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo)
Using package ModelicaServices with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo)
Running command: translateModel(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ModelicaTest_3.2.1_ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4")
translateModel(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ModelicaTest_3.2.1_ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo): time 0.001178/0.001178, allocations: 104.5 kB / 16.42 MB, free: 6.492 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo): time 0.001135/0.001135, allocations: 192.2 kB / 17.35 MB, free: 5.754 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo): time 1.246/1.246, allocations: 205.1 MB / 223.2 MB, free: 12.24 MB / 190.1 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaTest 3.2.1+maint.om/package.mo): time 0.1548/0.1548, allocations: 38 MB / 308.6 MB, free: 6.004 MB / 254.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 1.799e-05/1.8e-05, allocations: 2.281 kB / 433.6 MB, free: 14.5 MB / 318.1 MB
Notification: Performance of NFInst.instantiate(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4): time 0.2866/0.2866, allocations: 101.8 MB / 0.5229 GB, free: 4.359 MB / 398.1 MB
Notification: Performance of NFInst.instExpressions: time 0.03982/0.3264, allocations: 39.05 MB / 0.561 GB, free: 3.539 MB / 398.1 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.002602/0.3291, allocations: 96.53 kB / 0.5611 GB, free: 3.539 MB / 398.1 MB
Notification: Performance of NFTyping.typeComponents: time 0.002708/0.3318, allocations: 1.235 MB / 0.5623 GB, free: 3.52 MB / 398.1 MB
Notification: Performance of NFTyping.typeBindings: time 0.01917/0.351, allocations: 8.254 MB / 0.5704 GB, free: 0.6328 MB / 398.1 MB
Notification: Performance of NFTyping.typeClassSections: time 0.01784/0.3689, allocations: 8.07 MB / 0.5783 GB, free: 12.39 MB / 414.1 MB
Notification: Performance of NFFlatten.flatten: time 0.009336/0.3783, allocations: 8.335 MB / 0.5864 GB, free: 5.434 MB / 414.1 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.002148/0.3804, allocations: 1.579 MB / 0.588 GB, free: 3.871 MB / 414.1 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.004624/0.3851, allocations: 3.207 MB / 0.5911 GB, free: 0.9258 MB / 414.1 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.02298/0.4081, allocations: 12.14 MB / 0.603 GB, free: 4.926 MB / 430.1 MB
Notification: Performance of NFPackage.collectConstants: time 0.0007164/0.4088, allocations: 224 kB / 0.6032 GB, free: 4.707 MB / 430.1 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.01919/0.428, allocations: 10.03 MB / 0.613 GB, free: 10.84 MB / 446.1 MB
Notification: Performance of combineBinaries: time 0.00541/0.4334, allocations: 5.175 MB / 0.618 GB, free: 5.918 MB / 446.1 MB
Notification: Performance of replaceArrayConstructors: time 0.002432/0.4359, allocations: 3.353 MB / 0.6213 GB, free: 2.699 MB / 446.1 MB
Notification: Performance of NFVerifyModel.verify: time 0.0007132/0.4366, allocations: 426.8 kB / 0.6217 GB, free: 2.281 MB / 446.1 MB
Notification: Performance of FrontEnd: time 0.0003787/0.437, allocations: 59.75 kB / 0.6218 GB, free: 2.223 MB / 446.1 MB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 536 (362)
 * Number of variables: 636 (432)
Notification: Performance of Bindings: time 0.01351/0.4505, allocations: 15.2 MB / 0.6366 GB, free: 2.914 MB / 462.1 MB
Notification: Performance of FunctionAlias: time 0.001558/0.4521, allocations: 1.594 MB / 0.6382 GB, free: 1.348 MB / 462.1 MB
Notification: Performance of Early Inline: time 0.007905/0.46, allocations: 8.024 MB / 0.646 GB, free: 9.555 MB / 478.1 MB
Notification: Performance of simplify1: time 0.0007611/0.4608, allocations: 0.5267 MB / 0.6465 GB, free: 9.066 MB / 478.1 MB
Notification: Performance of Alias: time 0.006122/0.4669, allocations: 5.877 MB / 0.6522 GB, free: 2.906 MB / 478.1 MB
Notification: Performance of simplify2: time 0.0005852/0.4675, allocations: 0.5071 MB / 0.6527 GB, free: 2.434 MB / 478.1 MB
Notification: Performance of Events: time 0.001668/0.4692, allocations: 1.803 MB / 0.6545 GB, free: 0.6641 MB / 478.1 MB
Notification: Performance of Detect States: time 0.001671/0.4709, allocations: 1.945 MB / 0.6564 GB, free: 14.76 MB / 494.1 MB
Notification: Performance of Partitioning: time 0.003093/0.474, allocations: 3.021 MB / 0.6593 GB, free: 11.46 MB / 494.1 MB
Error: Internal error NBAdjacency.Matrix.create failed to create adjacency matrix for system:
System Variables (409/614)
****************************
(1)       [ALGB] (1) Real pipe2.state_b.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(2)       [ALGB] (1) Real[1] pipe2.mb_flows (min = {-1e5 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1})
(3)       [DISC] (1) Integer sink.medium.phase (fixed = false, start = 1, min = 0, max = 2)
(4)       [ALGB] (1) protected Real valveIncompressible1.state_a.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(5)       [ALGB] (1) Real[1] pipe2.mediums.T (start = {pipe2.T_start}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}, StateSelect = default)
(6)       [ALGB] (1) Real pipe2.state_b.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(7)       [DISC] (9) Integer[3, 3] pipe1.statesFM.phase (min = {0 for $i1 in 1:3}, max = {2 for $i1 in 1:3})
(8)       [ALGB] (2) Real[2] pipe3.H_flows (min = {-1e8 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1000.0 for $i1 in 1:2})
(9)       [DISC] (4) Integer[2, 2] pipe2.statesFM.phase (min = {0 for $i1 in 1:2}, max = {2 for $i1 in 1:2})
(10)      [ALGB] (1) protected Real[1] pipe3.dheightsFM
(11)      [DISC] (1) final input Integer[1, 1] pipe3.heatTransfer.states.phase = {pipe3.mediums[1].state.phase} (min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1})
(12)      [DISC] (1) protected Real valveOpening1.b
(13)      [ALGB] (2) Real[2] pipe2.H_flows (min = {-1e8 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1000.0 for $i1 in 1:2})
(14)      [DISC] (1) protected Real valveOpening1.a
(15)      [ALGB] (2) Real[2] pipe1.H_flows (min = {-1e8 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1000.0 for $i1 in 1:2})
(16)      [DISC] (1) Integer[1] pipe3.mediums.phase (fixed = {false for $i1 in 1:1}, start = {1 for $i1 in 1:1}, min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1})
(17)      [ALGB] (1) final Real[1] pipe3.flowModel.dheights = pipe3.dheightsFM
(18)      [DISC] (1) protected discrete Real valveOpening1.nextEvent (fixed = true, start = 0.0)
(19)      [ALGB] (2) final Real[2] pipe1.flowModel.dheights = pipe1.dheightsFM
(20)      [ALGB] (1) Real pipe2.state_b.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(21)      [DER-] (1) Real $DER.splitter.U
(22)      [ALGB] (1) stream Real pipe1.port_b.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(23)      [DER-] (1) Real[1] $DER.pipe3.Us
(24)      [ALGB] (1) Real[1] pipe2.mediums.T_degC = {Modelica.SIunits.Conversions.to_degC(pipe2.mediums[1].T)}
(25)      [ALGB] (1) Real[1] pipe3.mediums.T_degC = {Modelica.SIunits.Conversions.to_degC(pipe3.mediums[1].T)}
(26)      [ALGB] (3) final Real[3] pipe1.flowModel.crossAreas = pipe1.crossAreasFM
(27)      [ALGB] (3) final Real[3] pipe1.flowModel.dimensions = pipe1.dimensionsFM
(28)      [ALGB] (1) Real[1] pipe1.Qb_flows
(29)      [ALGB] (1) Real pipe3.port_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(30)      [ALGB] (1) Real pipe2.state_a.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(31)      [ALGB] (1) final input Real[1, 1] pipe2.heatTransfer.states.T = {pipe2.mediums[1].state.T} (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(32)      [ALGB] (1) Real splitter.medium.sat.psat (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(33)      [DER-] (1) Real[1] $DER.pipe2.Us
(34)      [ALGB] (1) Real pipe2.state_a.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(35)      [DISC] (9) final input Integer[3, 3] pipe1.flowModel.states.phase = {pipe1.statesFM[1].phase, pipe1.statesFM[2].phase, pipe1.statesFM[3].phase} (min = {0 for $i1 in 1:3}, max = {2 for $i1 in 1:3})
(36)      [DER-] (1) Real $DER.splitter.m
(37)      [ALGB] (1) Real[1] pipe1.mediums.state.T (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(38)      [ALGB] (1) Real pipe2.state_a.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(39)      [ALGB] (1) Real[1] pipe2.mediums.sat.Tsat (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(40)      [ALGB] (1) Real valveIncompressible1.port_a_T = Modelica.Fluid.Utilities.regStep(-valveIncompressible1.port_b.m_flow, ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible1.Medium.temperature(valveIncompressible1.state_a), ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible1.Medium.temperature(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible1.Medium.setState_phX(pipe3.port_b.p, valveIncompressible1.port_a.h_outflow, {}, 0, 0)), valveIncompressible1.m_flow_small) (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(41)      [DER-] (1) Real[1] $DER.pipe1.Us
(42)      [ALGB] (1) stream Real valveIncompressible.port_b.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(43)      [ALGB] (1) final input Real[1, 1] pipe2.heatTransfer.states.d = {pipe2.mediums[1].state.d} (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(44)      [DISC] (1) Integer[1] pipe2.mediums.phase (fixed = {false for $i1 in 1:1}, start = {1 for $i1 in 1:1}, min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1})
(45)      [ALGB] (2) Real[2] pipe2.flowModel.mus = {ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.pipe2.flowModel.Medium.dynamicViscosity(pipe2.flowModel.states[$i1]) for $i1 in 1:2} (start = {0.001 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {0.001 for $i1 in 1:2})
(46)      [ALGB] (2) final Real[2] pipe2.flowModel.roughnesses = pipe2.roughnessesFM (min = {0.0 for $i1 in 1:2})
(47)      [ALGB] (1) final input Real[1, 1] pipe2.heatTransfer.states.h = {pipe2.mediums[1].state.h} (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1})
(48)      [DISC] (1) Integer[1] pipe2.mediums.state.phase (min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1})
(49)      [ALGB] (1) final Real[1] pipe2.fluidVolumes = {pipe2.crossAreas[1] * 10.0} .* pipe2.nParallel
(50)      [ALGB] (1) protected Real[1] pipe2.pathLengths
(51)      [ALGB] (1) Real[1] pipe1.mediums.state.d (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(52)      [ALGB] (1) Real pipe2.state_a.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(53)      [DISC] (1) Integer pipe2.state_a.phase (min = 0, max = 2)
(54)      [ALGB] (1) protected Real[1] pipe2.dheightsFM
(55)      [ALGB] (1) Real[1] pipe1.mediums.state.h (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1})
(56)      [ALGB] (1) final input Real[1, 1] pipe2.heatTransfer.states.p = {pipe2.mediums[1].state.p} (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(57)      [ALGB] (1) protected Real valveIncompressible.state_a.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(58)      [ALGB] (1) final input Real[1, 1] pipe3.heatTransfer.states.p = {pipe3.mediums[1].state.p} (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(59)      [ALGB] (1) Real valveIncompressible1.port_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(60)      [DISC] (1) protected Integer valveIncompressible1.state_a.phase (min = 0, max = 2)
(61)      [ALGB] (1) flow Real pipe1.port_a.m_flow (min = -1e60, max = 1e5)
(62)      [ALGB] (1) Real[1] pipe1.mediums.state.p (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(63)      [ALGB] (1) final input Real[1, 1] pipe3.heatTransfer.states.h = {pipe3.mediums[1].state.h} (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1})
(64)      [ALGB] (1) Real[1] pipe1.Hb_flows
(65)      [ALGB] (1) final input Real[1, 1] pipe3.heatTransfer.states.d = {pipe3.mediums[1].state.d} (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(66)      [ALGB] (1) protected Real valveIncompressible.state_a.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(67)      [ALGB] (1) Real[1] pipe2.heatTransfer.heatPorts.T (start = {288.15 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(68)      [ALGB] (1) protected Real valveIncompressible.state_a.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(69)      [ALGB] (1) protected Real valveIncompressible1.relativeFlowCoefficient
(70)      [ALGB] (2) final Real[2] pipe3.flowModel.crossAreas = pipe3.crossAreasFM
(71)      [ALGB] (2) final Real[2] pipe3.flowModel.dimensions = pipe3.dimensionsFM
(72)      [DISC] (1) Integer source.medium.state.phase (min = 0, max = 2)
(73)      [ALGB] (1) protected Real valveIncompressible.state_a.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(74)      [ALGB] (1) Real valveIncompressible1.port_b_T = Modelica.Fluid.Utilities.regStep(valveIncompressible1.port_b.m_flow, ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible1.Medium.temperature(valveIncompressible1.state_b), ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible1.Medium.temperature(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible1.Medium.setState_phX(valveIncompressible1.port_b.p, valveIncompressible1.port_b.h_outflow, {}, 0, 0)), valveIncompressible1.m_flow_small) (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(75)      [ALGB] (1) final input Real[1, 1] pipe3.heatTransfer.states.T = {pipe3.mediums[1].state.T} (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(76)      [ALGB] (1) Real source.medium.T_degC = Modelica.SIunits.Conversions.to_degC(-((-273.15) - source.medium.T_degC))
(77)      [DISC] (1) Integer[1] pipe1.mediums.state.phase (min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1})
(78)      [ALGB] (1) Real[1] pipe3.flowModel.mus_act (start = {0.001 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {0.001 for $i1 in 1:1})
(79)      [DISC] (1) protected Integer valveIncompressible.state_a.phase (min = 0, max = 2)
(80)      [ALGB] (2) Real[2] pipe1.flowModel.Fs_fg
(81)      [ALGB] (1) Real source.medium.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(82)      [ALGB] (1) protected Real valveIncompressible.state_b.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(83)      [ALGB] (1) Real valveIncompressible1.dp_turbulent = max(valveIncompressible1.dp_small, ((ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible1.Medium.dynamicViscosity(valveIncompressible1.state_a) + ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible1.Medium.dynamicViscosity(valveIncompressible1.state_b)) ^ 2.0 * 3.141592653589793 * 1.6e7) / (8.0 * valveIncompressible1.Av * max(valveIncompressible1.relativeFlowCoefficient, 0.001) * (ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible1.Medium.density(valveIncompressible1.state_b) + ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible1.Medium.density(valveIncompressible1.state_a)))) (min = 0.0, nominal = 1e5)
(84)      [ALGB] (1) Real valveIncompressible.dp_turbulent = max(valveIncompressible.dp_small, ((ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible.Medium.dynamicViscosity(valveIncompressible.state_a) + ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible.Medium.dynamicViscosity(valveIncompressible.state_b)) ^ 2.0 * 3.141592653589793 * 1.6e7) / (8.0 * valveIncompressible.Av * max(valveIncompressible.relativeFlowCoefficient, 0.001) * (ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible.Medium.density(valveIncompressible.state_b) + ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible.Medium.density(valveIncompressible.state_a)))) (min = 0.0, nominal = 1e5)
(85)      [DISC] (1) Integer sink.medium.state.phase (min = 0, max = 2)
(86)      [ALGB] (1) Real[1] pipe2.flowModel.Ib_flows
(87)      [ALGB] (1) Real valveIncompressible.dp (start = valveIncompressible.dp_start)
(88)      [ALGB] (2) Real[2] pipe3.m_flows (start = {0.0 for $i1 in 1:2}, min = {-1e60 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2})
(89)      [ALGB] (1) Real[1] pipe2.heatTransfer.Q_flows
(90)      [ALGB] (2) protected Real[2] pipe1.dheightsFM
(91)      [ALGB] (2) Real[2] pipe2.m_flows (start = {0.0 for $i1 in 1:2}, min = {-1e60 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2})
(92)      [ALGB] (1) Real[1] pipe2.flowModel.Is
(93)      [ALGB] (1) Real source.medium.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(94)      [ALGB] (1) protected Real valveIncompressible.state_b.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(95)      [ALGB] (2) Real[2] pipe1.m_flows (start = {0.0 for $i1 in 1:2}, min = {-1e60 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2})
(96)      [ALGB] (1) Real source.medium.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(97)      [ALGB] (1) protected Real valveIncompressible.state_b.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(98)      [ALGB] (1) flow Real pipe1.port_b.m_flow (min = -1e5, max = 1e60)
(99)      [ALGB] (1) Real[1] pipe3.flowModel.m_flows (start = {0.0 for $i1 in 1:1}, min = {-1e60 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, StateSelect = default)
(100)     [DISC] (1) Boolean $TEV_1
(101)     [ALGB] (1) Real[1] pipe1.heatTransfer.heatPorts.T (start = {288.15 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(102)     [DISC] (1) Boolean $TEV_0
(103)     [DISC] (1) Boolean[1] $SEV_15[$i1]
(104)     [ALGB] (1) protected Real valveIncompressible.state_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(105)     [ALGB] (1) flow Real valveIncompressible1.port_b.m_flow (min = -1e5, max = 1e60)
(106)     [ALGB] (2) protected Real[2] pipe1.pathLengths
(107)     [ALGB] (2) Real[2] pipe1.flowModel.rhos_act (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(108)     [ALGB] (1) Real[1] pipe1.mediums.T_degC = {Modelica.SIunits.Conversions.to_degC(pipe1.mediums[1].T)}
(109)     [DISC] (1) Integer[1] pipe3.mediums.state.phase (min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1})
(110)     [ALGB] (1) Real[1] pipe1.mediums.sat.psat (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(111)     [ALGB] (1) flow Real pipe3.port_a.m_flow (min = -1e60, max = 1e5)
(112)     [ALGB] (1) Real[1] pipe3.mb_flows (min = {-1e5 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1})
(113)     [ALGB] (4) final input Real[2, 2] pipe2.flowModel.states.T = {pipe2.statesFM[1].T, pipe2.statesFM[2].T} (start = {500.0 for $i1 in 1:2}, min = {273.15 for $i1 in 1:2}, max = {2273.15 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(114)     [ALGB] (1) Real[1] pipe2.flowModel.m_flows (start = {0.0 for $i1 in 1:1}, min = {-1e60 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, StateSelect = default)
(115)     [ALGB] (2) protected Real[2] pipe2.dimensionsFM
(116)     [ALGB] (2) protected Real[2] pipe2.crossAreasFM
(117)     [ALGB] (1) Real splitter.medium.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0, StateSelect = default)
(118)     [ALGB] (1) protected Real[1] pipe3.pathLengths
(119)     [ALGB] (1) stream Real valveIncompressible1.port_b.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(120)     [ALGB] (9) final input Real[3, 3] pipe1.flowModel.states.p = {pipe1.statesFM[1].p, pipe1.statesFM[2].p, pipe1.statesFM[3].p} (start = {5e6 for $i1 in 1:3}, min = {611.657 for $i1 in 1:3}, max = {1e8 for $i1 in 1:3}, nominal = {1e6 for $i1 in 1:3})
(121)     [ALGB] (1) flow Real valveIncompressible.port_b.m_flow (min = -1e5, max = 1e60)
(122)     [ALGB] (4) Real[2, 2] pipe3.statesFM.p (start = {5e6 for $i1 in 1:2}, min = {611.657 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2})
(123)     [ALGB] (1) Real[1] pipe1.Wb_flows
(124)     [ALGB] (9) final input Real[3, 3] pipe1.flowModel.states.h = {pipe1.statesFM[1].h, pipe1.statesFM[2].h, pipe1.statesFM[3].h} (start = {1e5 for $i1 in 1:3}, min = {-1e10 for $i1 in 1:3}, max = {1e10 for $i1 in 1:3}, nominal = {5e5 for $i1 in 1:3})
(125)     [ALGB] (4) final input Real[2, 2] pipe2.flowModel.states.d = {pipe2.statesFM[1].d, pipe2.statesFM[2].d} (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(126)     [ALGB] (1) Real[1] pipe2.flowModel.Fs_fg
(127)     [ALGB] (4) Real[2, 2] pipe3.statesFM.h (start = {1e5 for $i1 in 1:2}, min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {5e5 for $i1 in 1:2})
(128)     [ALGB] (1) Real splitter.medium.u (min = -1e8, max = 1e8, nominal = 1e6)
(129)     [ALGB] (9) final input Real[3, 3] pipe1.flowModel.states.d = {pipe1.statesFM[1].d, pipe1.statesFM[2].d, pipe1.statesFM[3].d} (start = {150.0 for $i1 in 1:3}, min = {0.0 for $i1 in 1:3}, max = {1e5 for $i1 in 1:3}, nominal = {500.0 for $i1 in 1:3})
(130)     [ALGB] (4) final input Real[2, 2] pipe2.flowModel.states.h = {pipe2.statesFM[1].h, pipe2.statesFM[2].h} (start = {1e5 for $i1 in 1:2}, min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {5e5 for $i1 in 1:2})
(131)     [ALGB] (4) Real[2, 2] pipe3.statesFM.d (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(132)     [ALGB] (1) Real[1] pipe1.vs = {(0.5 * (pipe1.m_flows[2] + pipe1.m_flows[1])) / (pipe1.crossAreas[1] * pipe1.mediums[1].d)} / pipe1.nParallel
(133)     [ALGB] (1) Real splitter.medium.T_degC = Modelica.SIunits.Conversions.to_degC(-((-273.15) - splitter.medium.T_degC))
(134)     [ALGB] (4) final input Real[2, 2] pipe2.flowModel.states.p = {pipe2.statesFM[1].p, pipe2.statesFM[2].p} (start = {5e6 for $i1 in 1:2}, min = {611.657 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2})
(135)     [ALGB] (1) flow Real[1] pipe3.heatTransfer.heatPorts.Q_flow
(136)     [ALGB] (1) Real source.medium.sat.psat (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(137)     [DISC] (1) final input Integer[1, 1] pipe2.heatTransfer.states.phase = {pipe2.mediums[1].state.phase} (min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1})
(138)     [ALGB] (1) Real[1] pipe2.Qb_flows
(139)     [ALGB] (1) Real splitter.mb_flow
(140)     [ALGB] (9) final input Real[3, 3] pipe1.flowModel.states.T = {pipe1.statesFM[1].T, pipe1.statesFM[2].T, pipe1.statesFM[3].T} (start = {500.0 for $i1 in 1:3}, min = {273.15 for $i1 in 1:3}, max = {2273.15 for $i1 in 1:3}, nominal = {500.0 for $i1 in 1:3})
(141)     [ALGB] (1) Real[1] pipe2.vs = {(0.5 * (pipe2.m_flows[2] + pipe2.m_flows[1])) / (pipe2.crossAreas[1] * pipe2.mediums[1].d)} / pipe2.nParallel
(142)     [ALGB] (1) Real[1] pipe3.mediums.u (min = {-1e8 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(143)     [ALGB] (4) Real[2, 2] pipe3.statesFM.T (start = {500.0 for $i1 in 1:2}, min = {273.15 for $i1 in 1:2}, max = {2273.15 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(144)     [ALGB] (1) Real[1] pipe2.flowModel.mus_act (start = {0.001 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {0.001 for $i1 in 1:1})
(145)     [ALGB] (2) final Real[2] pipe2.flowModel.vs = pipe2.vsFM
(146)     [ALGB] (1) Real[1] pipe3.mediums.state.p (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(147)     [ALGB] (1) Real[1] pipe3.mediums.p (start = {pipe3.ps_start[1]}, min = {0.0 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1}, StateSelect = prefer)
(148)     [ALGB] (1) Real[1] pipe2.flowModel.pathLengths_internal = pipe2.flowModel.pathLengths
(149)     [ALGB] (1) final Real[1] pipe1.heatTransfer.vs = pipe1.vs
(150)     [ALGB] (1) Real valveIncompressible.V_flow = (-valveIncompressible.port_b.m_flow) / Modelica.Fluid.Utilities.regStep(-valveIncompressible.port_b.m_flow, ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible.Medium.density(valveIncompressible.state_a), ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible.Medium.density(valveIncompressible.state_b), valveIncompressible.m_flow_small)
(151)     [ALGB] (1) Real[1] pipe3.vs = {(0.5 * (pipe3.m_flows[2] + pipe3.m_flows[1])) / (pipe3.crossAreas[1] * pipe3.mediums[1].d)} / pipe3.nParallel
(152)     [ALGB] (1) Real[1] pipe3.mediums.state.h (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1})
(153)     [ALGB] (1) Real[1] pipe3.mediums.h (start = {pipe3.h_start}, StateSelect = prefer)
(154)     [ALGB] (1) Real[1] pipe2.flowModel.rhos_act (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(155)     [ALGB] (2) Real[2] pipe3.flowModel.rhos = {ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.pipe3.flowModel.Medium.density(pipe3.flowModel.states[$i1]) for $i1 in 1:2} (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(156)     [ALGB] (1) Real[1] pipe3.mediums.state.d (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(157)     [ALGB] (1) Real[1] pipe3.mediums.d (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}, StateSelect = default)
(158)     [ALGB] (1) Real sink.medium.T_degC = Modelica.SIunits.Conversions.to_degC(-((-273.15) - sink.medium.T_degC))
(159)     [ALGB] (1) Real pipe3.state_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(160)     [ALGB] (1) Real[1] pipe3.flowModel.Fs_p
(161)     [ALGB] (1) protected Real valveIncompressible.relativeFlowCoefficient
(162)     [ALGB] (2) Real[2] pipe1.flowModel.Res_turbulent_internal = pipe1.flowModel.Re_turbulent * {1.0 for $i1 in 1:2}
(163)     [DISC] (1) protected Integer valveOpening2.last (start = 1)
(164)     [ALGB] (1) Real pipe3.state_b.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(165)     [ALGB] (4) Real[2, 2] pipe2.statesFM.p (start = {5e6 for $i1 in 1:2}, min = {611.657 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2})
(166)     [ALGB] (1) Real[1] pipe3.mediums.state.T (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(167)     [ALGB] (1) Real[1] pipe3.mediums.T (start = {pipe3.T_start}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}, StateSelect = default)
(168)     [ALGB] (1) Real pipe3.state_b.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(169)     [ALGB] (1) protected Real[1] pipe2.flowModel.diameters = 0.5 * (pipe2.flowModel.dimensions[2:2] + pipe2.flowModel.dimensions[1:1])
(170)     [ALGB] (4) Real[2, 2] pipe2.statesFM.h (start = {1e5 for $i1 in 1:2}, min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {5e5 for $i1 in 1:2})
(171)     [ALGB] (1) Real[1] pipe2.Hb_flows
(172)     [ALGB] (2) Real[2] pipe1.flowModel.Ib_flows
(173)     [ALGB] (4) Real[2, 2] pipe2.statesFM.d (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(174)     [ALGB] (1) Real[1] pipe2.flowModel.Res_turbulent_internal = pipe2.flowModel.Re_turbulent * {1.0 for $i1 in 1:1}
(175)     [ALGB] (1) Real pipe3.state_b.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(176)     [ALGB] (1) Real[1] pipe1.mediums.u (min = {-1e8 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(177)     [ALGB] (1) Real sink.medium.sat.psat (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(178)     [DISC] (1) Boolean $SEV_9
(179)     [DISC] (1) Boolean $SEV_8
(180)     [ALGB] (1) Real[1] pipe1.mediums.p (start = {pipe1.ps_start[1]}, min = {0.0 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1}, StateSelect = prefer)
(181)     [DISC] (1) Integer splitter.medium.state.phase (min = 0, max = 2)
(182)     [ALGB] (1) Real[1] pipe3.heatTransfer.Ts = {ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.pipe3.heatTransfer.Medium.temperature(pipe3.heatTransfer.states[1])} (start = {288.15 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(183)     [ALGB] (4) Real[2, 2] pipe2.statesFM.T (start = {500.0 for $i1 in 1:2}, min = {273.15 for $i1 in 1:2}, max = {2273.15 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(184)     [ALGB] (1) Real[1] pipe1.heatTransfer.Q_flows
(185)     [ALGB] (3) protected Real[3] pipe1.roughnessesFM (min = {0.0 for $i1 in 1:3})
(186)     [ALGB] (1) flow Real[1] source.ports.m_flow (min = {-1e60}, max = {1e60})
(187)     [ALGB] (1) Real[1] pipe1.mediums.h (start = {pipe1.h_start}, StateSelect = prefer)
(188)     [ALGB] (1) Real source.medium.u (min = -1e8, max = 1e8, nominal = 1e6)
(189)     [ALGB] (1) Real pipe3.state_a.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(190)     [ALGB] (1) Real[1] pipe1.mediums.d (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}, StateSelect = default)
(191)     [ALGB] (1) Real pipe1.port_a.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(192)     [DISC] (1) protected Integer valveOpening1.last (start = 1)
(193)     [ALGB] (1) Real pipe1.state_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(194)     [ALGB] (1) Real[1] pipe3.flowModel.dps_fg (start = {pipe3.flowModel.p_a_start - pipe3.flowModel.p_b_start for $i1 in 1:1})
(195)     [ALGB] (1) final Real[1] pipe3.fluidVolumes = {pipe3.crossAreas[1] * 10.0} .* pipe3.nParallel
(196)     [ALGB] (1) Real[1] pipe3.mediums.sat.psat (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(197)     [ALGB] (2) protected Real[2] pipe1.flowModel.diameters = 0.5 * (pipe1.flowModel.dimensions[2:3] + pipe1.flowModel.dimensions[1:2])
(198)     [ALGB] (1) Real pipe3.state_a.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(199)     [ALGB] (1) Real[1] pipe3.flowModel.pathLengths_internal = pipe3.flowModel.pathLengths
(200)     [ALGB] (1) Real pipe1.state_b.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(201)     [ALGB] (1) Real pipe3.state_a.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(202)     [DISC] (1) Integer splitter.medium.phase (fixed = false, start = 1, min = 0, max = 2)
(203)     [ALGB] (1) Real source.medium.h (StateSelect = default)
(204)     [DISC] (1) protected discrete Real valveOpening1.nextEventScaled (fixed = true, start = 0.0)
(205)     [ALGB] (1) stream Real splitter.port_3.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(206)     [ALGB] (3) protected Real[3] pipe1.vsFM
(207)     [ALGB] (2) Real[2] pipe1.flowModel.m_flows (start = {0.0 for $i1 in 1:2}, min = {-1e60 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, StateSelect = default)
(208)     [ALGB] (1) Real[1] pipe1.mediums.T (start = {pipe1.T_start}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}, StateSelect = default)
(209)     [ALGB] (1) Real pipe1.state_b.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(210)     [ALGB] (1) Real source.medium.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0, StateSelect = default)
(211)     [ALGB] (2) protected Real[2] pipe2.roughnessesFM (min = {0.0 for $i1 in 1:2})
(212)     [ALGB] (1) stream Real valveIncompressible.port_a.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(213)     [ALGB] (1) Real[1] pipe1.heatTransfer.Ts = {ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.pipe1.heatTransfer.Medium.temperature(pipe1.heatTransfer.states[1])} (start = {288.15 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(214)     [ALGB] (9) Real[3, 3] pipe1.statesFM.p (start = {5e6 for $i1 in 1:3}, min = {611.657 for $i1 in 1:3}, max = {1e8 for $i1 in 1:3}, nominal = {1e6 for $i1 in 1:3})
(215)     [ALGB] (1) Real pipe3.state_a.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(216)     [DER-] (1) Real[1] $DER.pipe3.ms
(217)     [DISC] (1) protected discrete Real valveOpening2.nextEvent (fixed = true, start = 0.0)
(218)     [DISC] (1) Boolean[1] $SEV_38[$i1]
(219)     [ALGB] (9) Real[3, 3] pipe1.statesFM.h (start = {1e5 for $i1 in 1:3}, min = {-1e10 for $i1 in 1:3}, max = {1e10 for $i1 in 1:3}, nominal = {5e5 for $i1 in 1:3})
(220)     [ALGB] (1) Real pipe1.state_b.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(221)     [ALGB] (1) Real[1] pipe3.flowModel.Ib_flows
(222)     [ALGB] (1) stream Real pipe2.port_a.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(223)     [ALGB] (9) Real[3, 3] pipe1.statesFM.d (start = {150.0 for $i1 in 1:3}, min = {0.0 for $i1 in 1:3}, max = {1e5 for $i1 in 1:3}, nominal = {500.0 for $i1 in 1:3})
(224)     [ALGB] (1) Real sink.medium.u (min = -1e8, max = 1e8, nominal = 1e6)
(225)     [ALGB] (2) final Real[2] pipe3.flowModel.roughnesses = pipe3.roughnessesFM (min = {0.0 for $i1 in 1:2})
(226)     [DER-] (1) Real[1] $DER.pipe2.ms
(227)     [ALGB] (1) stream Real pipe1.port_a.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(228)     [ALGB] (1) Real splitter.Hb_flow
(229)     [DISC] (4) Integer[2, 2] pipe3.statesFM.phase (min = {0 for $i1 in 1:2}, max = {2 for $i1 in 1:2})
(230)     [DISC] (4) final input Integer[2, 2] pipe3.flowModel.states.phase = {pipe3.statesFM[1].phase, pipe3.statesFM[2].phase} (min = {0 for $i1 in 1:2}, max = {2 for $i1 in 1:2})
(231)     [DISC] (1) Boolean $SEV_53
(232)     [ALGB] (1) Real sink.medium.h (StateSelect = default)
(233)     [ALGB] (1) Real[1] pipe2.mediums.state.p (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(234)     [ALGB] (1) Real pipe1.state_a.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(235)     [DISC] (1) Boolean $SEV_52
(236)     [ALGB] (9) Real[3, 3] pipe1.statesFM.T (start = {500.0 for $i1 in 1:3}, min = {273.15 for $i1 in 1:3}, max = {2273.15 for $i1 in 1:3}, nominal = {500.0 for $i1 in 1:3})
(237)     [ALGB] (1) Real[1] pipe3.heatTransfer.Q_flows
(238)     [DISC] (1) Boolean $SEV_51
(239)     [DER-] (1) Real[1] $DER.pipe1.ms
(240)     [DISC] (1) Boolean $SEV_50
(241)     [ALGB] (2) Real[2] pipe1.flowModel.mus_act (start = {0.001 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {0.001 for $i1 in 1:2})
(242)     [ALGB] (1) Real sink.medium.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0, StateSelect = default)
(243)     [ALGB] (2) protected Real[2] pipe2.vsFM
(244)     [ALGB] (1) Real[1] pipe2.mediums.state.h (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1})
(245)     [ALGB] (1) Real pipe1.state_a.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(246)     [ALGB] (2) protected Real[2] pipe3.roughnessesFM (min = {0.0 for $i1 in 1:2})
(247)     [ALGB] (1) Real[1] pipe2.mediums.state.d (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(248)     [ALGB] (1) Real pipe1.state_a.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(249)     [ALGB] (1) Real[1] pipe2.heatTransfer.Ts = {ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.pipe2.heatTransfer.Medium.temperature(pipe2.heatTransfer.states[1])} (start = {288.15 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(250)     [ALGB] (1) Real[1] pipe2.Wb_flows
(251)     [ALGB] (1) Real[1] pipe3.flowModel.Is
(252)     [ALGB] (1) final Real[1] pipe3.heatTransfer.vs = pipe3.vs
(253)     [ALGB] (1) Real[1] pipe1.mediums.sat.Tsat (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(254)     [DISC] (2) Boolean[2] $SEV_37[$i1]
(255)     [ALGB] (1) Real[1] pipe2.flowModel.dps_fg (start = {pipe2.flowModel.p_a_start - pipe2.flowModel.p_b_start for $i1 in 1:1})
(256)     [DISC] (1) Integer pipe1.state_b.phase (min = 0, max = 2)
(257)     [DISC] (1) Boolean $SEV_49
(258)     [DISC] (1) Boolean $SEV_48
(259)     [ALGB] (1) Real[1] pipe2.mediums.state.T (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(260)     [ALGB] (1) final Real[1] pipe2.flowModel.dheights = pipe2.dheightsFM
(261)     [ALGB] (1) Real pipe1.state_a.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(262)     [ALGB] (4) final input Real[2, 2] pipe3.flowModel.states.T = {pipe3.statesFM[1].T, pipe3.statesFM[2].T} (start = {500.0 for $i1 in 1:2}, min = {273.15 for $i1 in 1:2}, max = {2273.15 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(263)     [DISC] (1) Boolean $SEV_47
(264)     [DISC] (1) Boolean $SEV_46
(265)     [DISC] (1) Boolean $SEV_45
(266)     [ALGB] (1) Real[1] pipe1.mb_flows (min = {-1e5 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1})
(267)     [DISC] (1) Boolean $SEV_44
(268)     [DISC] (1) Boolean $SEV_43
(269)     [DISC] (1) Boolean $SEV_40
(270)     [ALGB] (2) final Real[2] pipe2.flowModel.dimensions = pipe2.dimensionsFM
(271)     [ALGB] (2) final Real[2] pipe2.flowModel.crossAreas = pipe2.crossAreasFM
(272)     [DISC] (1) protected discrete Real valveOpening2.nextEventScaled (fixed = true, start = 0.0)
(273)     [ALGB] (1) protected Real valveIncompressible.minLimiter.y
(274)     [DISC] (1) Integer source.medium.phase (fixed = false, start = 1, min = 0, max = 2)
(275)     [ALGB] (1) Real[1] pipe3.Qb_flows
(276)     [ALGB] (1) Real $FUN_9
(277)     [ALGB] (4) final input Real[2, 2] pipe3.flowModel.states.d = {pipe3.statesFM[1].d, pipe3.statesFM[2].d} (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(278)     [ALGB] (1) Real $FUN_8
(279)     [ALGB] (1) protected Real pipe3.flowModel.dp_fric_nominal = sum({ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.pipe3.flowModel.WallFriction.pressureLoss_m_flow(pipe3.flowModel.m_flow_nominal / pipe3.flowModel.nParallel, pipe3.flowModel.rho_nominal, pipe3.flowModel.rho_nominal, pipe3.flowModel.mu_nominal, pipe3.flowModel.mu_nominal, pipe3.flowModel.pathLengths_internal[1], pipe3.flowModel.diameters[1], ((pipe3.flowModel.crossAreas[2:2] + pipe3.flowModel.crossAreas[1:1]) / 2.0)[1], ((pipe3.flowModel.roughnesses[2:2] + pipe3.flowModel.roughnesses[1:1]) / 2.0)[1], pipe3.flowModel.m_flow_small / pipe3.flowModel.nParallel, pipe3.flowModel.Res_turbulent_internal[1])}) (min = 0.0, nominal = 1e5)
(280)     [ALGB] (1) Real $FUN_7
(281)     [ALGB] (1) Real $FUN_6
(282)     [ALGB] (1) Real $FUN_25
(283)     [ALGB] (1) final Real[1] pipe1.fluidVolumes = {pipe1.crossAreas[1] * 10.0} .* pipe1.nParallel
(284)     [ALGB] (1) Real $FUN_5
(285)     [ALGB] (4) final input Real[2, 2] pipe3.flowModel.states.h = {pipe3.statesFM[1].h, pipe3.statesFM[2].h} (start = {1e5 for $i1 in 1:2}, min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {5e5 for $i1 in 1:2})
(286)     [ALGB] (1) Real $FUN_4
(287)     [ALGB] (1) Real $FUN_23
(288)     [ALGB] (1) Real $FUN_3
(289)     [ALGB] (2) protected Real[2] pipe3.vsFM
(290)     [ALGB] (1) Real $FUN_2
(291)     [ALGB] (1) Real $FUN_21
(292)     [ALGB] (1) Real $FUN_1
(293)     [DISC] (1) Integer $FUN_20
(294)     [ALGB] (1) Real splitter.medium.sat.Tsat (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(295)     [ALGB] (4) final input Real[2, 2] pipe3.flowModel.states.p = {pipe3.statesFM[1].p, pipe3.statesFM[2].p} (start = {5e6 for $i1 in 1:2}, min = {611.657 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2})
(296)     [ALGB] (1) Real splitter.medium.p_bar = Modelica.SIunits.Conversions.to_bar(99999.99999999999 * splitter.medium.p_bar)
(297)     [DISC] (4) final input Integer[2, 2] pipe2.flowModel.states.phase = {pipe2.statesFM[1].phase, pipe2.statesFM[2].phase} (min = {0 for $i1 in 1:2}, max = {2 for $i1 in 1:2})
(298)     [ALGB] (2) protected Real[2] pipe3.crossAreasFM
(299)     [ALGB] (2) protected Real[2] pipe3.dimensionsFM
(300)     [ALGB] (1) Real[1] pipe2.mediums.sat.psat (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(301)     [DISC] (1) Boolean $SEV_36
(302)     [DISC] (1) Boolean $SEV_35
(303)     [DISC] (1) Boolean $SEV_34
(304)     [DISC] (1) Boolean $SEV_33
(305)     [DISC] (1) Boolean $SEV_32
(306)     [DISC] (1) Boolean $SEV_31
(307)     [ALGB] (2) Real[2] sink.ports.p (start = {5e6 for $i1 in 1:2}, min = {611.657 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2})
(308)     [DISC] (1) Boolean $SEV_30
(309)     [ALGB] (1) Real pipe2.port_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(310)     [ALGB] (1) protected Real valveIncompressible1.minLimiter.y
(311)     [ALGB] (1) flow Real pipe2.port_a.m_flow (min = -1e60, max = 1e5)
(312)     [ALGB] (1) Real $FUN_19
(313)     [ALGB] (1) Real $FUN_18
(314)     [ALGB] (1) Real $FUN_17
(315)     [DISC] (1) Integer $FUN_16
(316)     [ALGB] (1) Real $FUN_15
(317)     [ALGB] (1) Real[1] pipe3.flowModel.rhos_act (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(318)     [ALGB] (1) Real $FUN_14
(319)     [ALGB] (1) Real $FUN_13
(320)     [ALGB] (1) stream Real valveIncompressible1.port_a.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(321)     [ALGB] (1) Real $FUN_12
(322)     [ALGB] (1) Real sink.medium.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(323)     [ALGB] (1) Real $FUN_11
(324)     [DISC] (1) Integer pipe3.state_a.phase (min = 0, max = 2)
(325)     [ALGB] (1) Real $FUN_10
(326)     [ALGB] (1) final Real[1] pipe3.flowModel.pathLengths = pipe3.pathLengths
(327)     [ALGB] (1) Real sink.medium.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(328)     [ALGB] (1) Real[1] pipe3.Hb_flows
(329)     [ALGB] (3) final Real[3] pipe1.flowModel.roughnesses = pipe1.roughnessesFM (min = {0.0 for $i1 in 1:3})
(330)     [ALGB] (3) Real[3] pipe1.flowModel.mus = {ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.pipe1.flowModel.Medium.dynamicViscosity(pipe1.flowModel.states[$i1]) for $i1 in 1:3} (start = {0.001 for $i1 in 1:3}, min = {0.0 for $i1 in 1:3}, max = {1e8 for $i1 in 1:3}, nominal = {0.001 for $i1 in 1:3})
(331)     [ALGB] (1) Real splitter.medium.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(332)     [DISC] (1) Integer[1] pipe1.mediums.phase (fixed = {false for $i1 in 1:1}, start = {1 for $i1 in 1:1}, min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1})
(333)     [ALGB] (1) stream Real pipe3.port_a.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(334)     [DISC] (1) Boolean $SEV_29
(335)     [DISC] (1) Boolean $SEV_28
(336)     [ALGB] (1) final Real[1] pipe2.heatTransfer.vs = pipe2.vs
(337)     [DISC] (1) Boolean $SEV_27
(338)     [DISC] (1) Boolean $SEV_26
(339)     [DISC] (1) Boolean $SEV_25
(340)     [DISC] (1) Boolean $SEV_24
(341)     [ALGB] (2) final Real[2] pipe3.flowModel.vs = pipe3.vsFM
(342)     [ALGB] (1) Real splitter.medium.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(343)     [ALGB] (1) Real valveIncompressible.port_a_T = Modelica.Fluid.Utilities.regStep(-valveIncompressible.port_b.m_flow, ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible.Medium.temperature(valveIncompressible.state_a), ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible.Medium.temperature(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible.Medium.setState_phX(pipe2.port_b.p, valveIncompressible.port_a.h_outflow, {}, 0, 0)), valveIncompressible.m_flow_small) (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(344)     [DISC] (1) Boolean $SEV_21
(345)     [ALGB] (1) protected Real pipe1.flowModel.dp_fric_nominal = sum(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.pipe1.flowModel.WallFriction.pressureLoss_m_flow(pipe1.flowModel.m_flow_nominal / pipe1.flowModel.nParallel, pipe1.flowModel.rho_nominal, pipe1.flowModel.rho_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.pathLengths_internal[$i1], pipe1.flowModel.diameters[$i1], ((pipe1.flowModel.crossAreas[2:3] + pipe1.flowModel.crossAreas[1:2]) / 2.0)[$i1], ((pipe1.flowModel.roughnesses[2:3] + pipe1.flowModel.roughnesses[1:2]) / 2.0)[$i1], pipe1.flowModel.m_flow_small / pipe1.flowModel.nParallel, pipe1.flowModel.Res_turbulent_internal[$i1]) for $i1 in 1:2) (min = 0.0, nominal = 1e5)
(346)     [ALGB] (1) Real splitter.medium.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(347)     [ALGB] (2) flow Real[2] sink.ports.m_flow (min = {-1e60 for $ports1 in 1:2}, max = {1e60 for $ports1 in 1:2})
(348)     [ALGB] (1) Real sink.medium.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(349)     [ALGB] (1) Real[1] pipe3.flowModel.Res_turbulent_internal = pipe3.flowModel.Re_turbulent * {1.0 for $i1 in 1:1}
(350)     [ALGB] (2) Real[2] pipe1.flowModel.Is
(351)     [DISC] (1) final input Integer[1, 1] pipe1.heatTransfer.states.phase = {pipe1.mediums[1].state.phase} (min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1})
(352)     [ALGB] (1) Real[1] pipe3.mediums.p_bar = {Modelica.SIunits.Conversions.to_bar(pipe3.mediums[1].p)}
(353)     [ALGB] (2) stream Real[2] sink.ports.h_outflow (start = {1e5 for $i1 in 1:2}, min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {5e5 for $i1 in 1:2})
(354)     [ALGB] (1) Real splitter.medium.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(355)     [ALGB] (1) Real valveIncompressible.port_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(356)     [ALGB] (1) protected Real valveIncompressible1.state_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(357)     [ALGB] (1) Real[1] pipe3.flowModel.Fs_fg
(358)     [DISC] (1) Boolean $SEV_18
(359)     [DISC] (1) protected Integer valveIncompressible1.state_b.phase (min = 0, max = 2)
(360)     [DISC] (1) Boolean $SEV_17
(361)     [ALGB] (2) Real[2] pipe1.flowModel.dps_fg (start = {(pipe1.flowModel.p_a_start - pipe1.flowModel.p_b_start) / 2.0 for $i1 in 1:2})
(362)     [DISC] (1) Boolean $SEV_14
(363)     [DISC] (1) Boolean $SEV_13
(364)     [ALGB] (1) protected Real valveIncompressible1.state_b.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(365)     [DISC] (1) Boolean $SEV_10
(366)     [ALGB] (1) protected Real valveIncompressible1.state_b.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(367)     [ALGB] (1) Real[1] pipe3.mediums.sat.Tsat (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(368)     [ALGB] (1) Real valveIncompressible.port_b_T = Modelica.Fluid.Utilities.regStep(valveIncompressible.port_b.m_flow, ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible.Medium.temperature(valveIncompressible.state_b), ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible.Medium.temperature(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible.Medium.setState_phX(valveIncompressible.port_b.p, valveIncompressible.port_b.h_outflow, {}, 0, 0)), valveIncompressible.m_flow_small) (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(369)     [ALGB] (1) stream Real[1] source.ports.h_outflow (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1})
(370)     [ALGB] (3) protected Real[3] pipe1.dimensionsFM
(371)     [ALGB] (3) protected Real[3] pipe1.crossAreasFM
(372)     [ALGB] (1) protected Real valveIncompressible1.state_b.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(373)     [DISC] (1) protected Integer valveIncompressible.state_b.phase (min = 0, max = 2)
(374)     [ALGB] (1) flow Real[1] pipe1.heatTransfer.heatPorts.Q_flow
(375)     [ALGB] (1) Real[1] pipe2.flowModel.Fs_p
(376)     [ALGB] (2) Real[2] pipe1.flowModel.Fs_p
(377)     [ALGB] (1) Real[1] pipe3.heatTransfer.heatPorts.T (start = {288.15 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(378)     [ALGB] (1) final Real[1] pipe2.flowModel.pathLengths = pipe2.pathLengths
(379)     [DISC] (1) protected Real valveOpening2.b
(380)     [ALGB] (1) Real[1] pipe2.mediums.p_bar = {Modelica.SIunits.Conversions.to_bar(pipe2.mediums[1].p)}
(381)     [DISC] (1) protected Real valveOpening2.a
(382)     [ALGB] (2) Real[2] pipe2.flowModel.rhos = {ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.pipe2.flowModel.Medium.density(pipe2.flowModel.states[$i1]) for $i1 in 1:2} (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(383)     [ALGB] (3) Real[3] pipe1.flowModel.rhos = {ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.pipe1.flowModel.Medium.density(pipe1.flowModel.states[$i1]) for $i1 in 1:3} (start = {150.0 for $i1 in 1:3}, min = {0.0 for $i1 in 1:3}, max = {1e5 for $i1 in 1:3}, nominal = {500.0 for $i1 in 1:3})
(384)     [ALGB] (1) Real valveIncompressible1.V_flow = (-valveIncompressible1.port_b.m_flow) / Modelica.Fluid.Utilities.regStep(-valveIncompressible1.port_b.m_flow, ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible1.Medium.density(valveIncompressible1.state_a), ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveIncompressible1.Medium.density(valveIncompressible1.state_b), valveIncompressible1.m_flow_small)
(385)     [ALGB] (1) Real[1] pipe2.mediums.u (min = {-1e8 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(386)     [ALGB] (1) protected Real pipe2.flowModel.dp_fric_nominal = sum({ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.pipe2.flowModel.WallFriction.pressureLoss_m_flow(pipe2.flowModel.m_flow_nominal / pipe2.flowModel.nParallel, pipe2.flowModel.rho_nominal, pipe2.flowModel.rho_nominal, pipe2.flowModel.mu_nominal, pipe2.flowModel.mu_nominal, pipe2.flowModel.pathLengths_internal[1], pipe2.flowModel.diameters[1], ((pipe2.flowModel.crossAreas[2:2] + pipe2.flowModel.crossAreas[1:1]) / 2.0)[1], ((pipe2.flowModel.roughnesses[2:2] + pipe2.flowModel.roughnesses[1:1]) / 2.0)[1], pipe2.flowModel.m_flow_small / pipe2.flowModel.nParallel, pipe2.flowModel.Res_turbulent_internal[1])}) (min = 0.0, nominal = 1e5)
(387)     [ALGB] (1) final input Real[1, 1] pipe1.heatTransfer.states.p = {pipe1.mediums[1].state.p} (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(388)     [DISC] (1) Boolean[1] $SEV_19[$i1]
(389)     [DISC] (1) Integer pipe1.state_a.phase (min = 0, max = 2)
(390)     [ALGB] (1) protected Real valveIncompressible1.state_a.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(391)     [ALGB] (1) Real[1] source.ports.p (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(392)     [ALGB] (1) Real valveIncompressible1.dp (start = valveIncompressible1.dp_start)
(393)     [ALGB] (1) Real[1] pipe2.mediums.p (start = {pipe2.ps_start[1]}, min = {0.0 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1}, StateSelect = prefer)
(394)     [ALGB] (1) final input Real[1, 1] pipe1.heatTransfer.states.h = {pipe1.mediums[1].state.h} (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1})
(395)     [ALGB] (1) protected Real[1] pipe3.flowModel.diameters = 0.5 * (pipe3.flowModel.dimensions[2:2] + pipe3.flowModel.dimensions[1:1])
(396)     [ALGB] (2) Real[2] pipe3.flowModel.mus = {ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.pipe3.flowModel.Medium.dynamicViscosity(pipe3.flowModel.states[$i1]) for $i1 in 1:2} (start = {0.001 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {0.001 for $i1 in 1:2})
(397)     [ALGB] (1) protected Real valveIncompressible1.state_a.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(398)     [ALGB] (1) final input Real[1, 1] pipe1.heatTransfer.states.d = {pipe1.mediums[1].state.d} (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(399)     [ALGB] (1) flow Real[1] pipe2.heatTransfer.heatPorts.Q_flow
(400)     [ALGB] (1) Real[1] pipe2.mediums.h (start = {pipe2.h_start}, StateSelect = prefer)
(401)     [ALGB] (1) protected Real valveIncompressible1.state_a.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(402)     [ALGB] (1) Real[1] pipe2.mediums.d (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}, StateSelect = default)
(403)     [ALGB] (1) Real[1] pipe3.Wb_flows
(404)     [ALGB] (2) final Real[2] pipe1.flowModel.pathLengths = pipe1.pathLengths
(405)     [ALGB] (1) Real[1] pipe1.mediums.p_bar = {Modelica.SIunits.Conversions.to_bar(pipe1.mediums[1].p)}
(406)     [ALGB] (1) Real pipe2.state_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(407)     [ALGB] (3) final Real[3] pipe1.flowModel.vs = pipe1.vsFM
(408)     [ALGB] (2) Real[2] pipe1.flowModel.pathLengths_internal = pipe1.flowModel.pathLengths
(409)     [ALGB] (1) final input Real[1, 1] pipe1.heatTransfer.states.T = {pipe1.mediums[1].state.T} (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})


System Equations (373/514)
****************************
(1)       [SCAL] (1) $FUN_1 = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.pipe1.flowModel.WallFriction.massFlowRate_dp_staticHead(pipe1.flowModel.dps_fg[$i1], pipe1.flowModel.rhos[(1:2)[$i1]], pipe1.flowModel.rhos[(2:3)[$i1]], pipe1.flowModel.mus[(1:2)[$i1]], pipe1.flowModel.mus[(2:3)[$i1]], pipe1.flowModel.pathLengths_internal[$i1], pipe1.flowModel.diameters[$i1], (pipe1.flowModel.g * pipe1.flowModel.dheights)[$i1], ((pipe1.flowModel.crossAreas[1:2] + pipe1.flowModel.crossAreas[2:3]) / 2.0)[$i1], ((pipe1.flowModel.roughnesses[1:2] + pipe1.flowModel.roughnesses[2:3]) / 2.0)[$i1], pipe1.flowModel.dp_small / 2.0, pipe1.flowModel.Res_turbulent_internal[$i1]) ($RES_$AUX_431)
(2)       [ARRY] (1) pipe1.mediums.phase = pipe1.mediums.state.phase ($RES_SIM_255)
(3)       [ARRY] (1) pipe3.mediums.p_bar = {1e-5 * pipe3.mediums[1].p} ($RES_BND_380)
(4)       [SCAL] (1) $FUN_2 = sum(pipe1.flowModel.dps_fg) ($RES_$AUX_430)
(5)       [ARRY] (1) pipe1.mediums.d = pipe1.mediums.state.d ($RES_SIM_256)
(6)       [ARRY] (1) pipe3.mediums.T_degC = {(-273.15) + pipe3.mediums[1].T} ($RES_BND_381)
(7)       [ARRY] (1) pipe1.mediums.T = pipe1.mediums.state.T ($RES_SIM_257)
(8)       [ARRY] (2) pipe3.flowModel.vs = pipe3.vsFM ($RES_BND_382)
(9)       [ARRY] (1) pipe1.mediums.p = pipe1.mediums.state.p ($RES_SIM_258)
(10)      [ARRY] (2) pipe3.flowModel.crossAreas = pipe3.crossAreasFM ($RES_BND_383)
(11)      [ARRY] (1) pipe1.mediums.h = pipe1.mediums.state.h ($RES_SIM_259)
(12)      [ARRY] (2) pipe3.flowModel.dimensions = pipe3.dimensionsFM ($RES_BND_384)
(13)      [ARRY] (2) pipe3.flowModel.roughnesses = pipe3.roughnessesFM ($RES_BND_385)
(14)      [ARRY] (1) pipe3.flowModel.dheights = pipe3.dheightsFM ($RES_BND_386)
(15)      [ARRY] (1) pipe3.flowModel.pathLengths = pipe3.pathLengths ($RES_BND_387)
(16)      [FOR-] (2) ($RES_BND_388)
(16)      [----] for $i1 in 1:2 loop
(16)      [----]   [SCAL] (1) pipe3.flowModel.rhos[$i1] = pipe3.flowModel.states.d ($RES_BND_389)
(16)      [----] end for;
(17)      [SCAL] (1) sink.medium.phase = sink.medium.state.phase ($RES_SIM_177)
(18)      [SCAL] (1) sink.medium.d = sink.medium.state.d ($RES_SIM_178)
(19)      [SCAL] (1) -((-273.15) - sink.medium.T_degC) = sink.medium.state.T ($RES_SIM_179)
(20)      [SCAL] (1) $FUN_3 = semiLinear(pipe1.port_a.m_flow, source.ports[1].h_outflow, pipe1.mediums[1].h) ($RES_$AUX_429)
(21)      [SCAL] (1) $FUN_4 = semiLinear(pipe1.port_b.m_flow, splitter.port_3.h_outflow, pipe1.mediums[1].h) ($RES_$AUX_428)
(22)      [SCAL] (1) $FUN_5 = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.pipe2.flowModel.WallFriction.massFlowRate_dp_staticHead(pipe2.flowModel.dps_fg[1], pipe2.flowModel.rhos[1], pipe2.flowModel.rhos[2], pipe2.flowModel.mus[1], pipe2.flowModel.mus[2], pipe2.flowModel.pathLengths_internal[1], pipe2.flowModel.diameters[1], (pipe2.flowModel.g * pipe2.flowModel.dheights)[1], (0.5 .* (pipe2.flowModel.crossAreas[1:1] + pipe2.flowModel.crossAreas[2:2]))[1], (0.5 .* (pipe2.flowModel.roughnesses[1:1] + pipe2.flowModel.roughnesses[2:2]))[1], pipe2.flowModel.dp_small, pipe2.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_427)
(23)      [SCAL] (1) $FUN_6 = sum(pipe2.flowModel.dps_fg) ($RES_$AUX_426)
(24)      [SCAL] (1) $FUN_7 = semiLinear(pipe2.port_a.m_flow, splitter.port_3.h_outflow, pipe2.mediums[1].h) ($RES_$AUX_425)
(25)      [SCAL] (1) pipe1.mediums[1].u = pipe1.mediums[1].h - pipe1.mediums[1].p / pipe1.mediums[1].d ($RES_SIM_261)
(26)      [SCAL] (1) $FUN_8 = semiLinear(valveIncompressible.port_b.m_flow, valveIncompressible.port_a.h_outflow, pipe2.mediums[1].h) ($RES_$AUX_424)
(27)      [ARRY] (1) pipe1.mediums.sat.psat = pipe1.mediums.p ($RES_SIM_262)
(28)      [SCAL] (1) $FUN_9 = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.pipe3.flowModel.WallFriction.massFlowRate_dp_staticHead(pipe3.flowModel.dps_fg[1], pipe3.flowModel.rhos[1], pipe3.flowModel.rhos[2], pipe3.flowModel.mus[1], pipe3.flowModel.mus[2], pipe3.flowModel.pathLengths_internal[1], pipe3.flowModel.diameters[1], (pipe3.flowModel.g * pipe3.flowModel.dheights)[1], (0.5 .* (pipe3.flowModel.crossAreas[1:1] + pipe3.flowModel.crossAreas[2:2]))[1], (0.5 .* (pipe3.flowModel.roughnesses[1:1] + pipe3.flowModel.roughnesses[2:2]))[1], pipe3.flowModel.dp_small, pipe3.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_423)
(29)      [SCAL] (1) pipe1.state_a.phase = 0 ($RES_SIM_437)
(30)      [SCAL] (1) pipe1.mediums[1].sat.Tsat = Modelica.Media.Water.IF97_Utilities.BaseIF97.Basic.tsat(pipe1.mediums[1].p) ($RES_SIM_263)
(31)      [SCAL] (1) $FUN_10 = sum(pipe3.flowModel.dps_fg) ($RES_$AUX_422)
(32)      [SCAL] (1) pipe1.state_a.h = source.ports[1].h_outflow ($RES_SIM_438)
(33)      [SCAL] (1) pipe1.mediums[1].T = Modelica.Media.Water.IF97_Utilities.T_props_ph(pipe1.mediums[1].p, pipe1.mediums[1].h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(pipe1.mediums[1].p, pipe1.mediums[1].h, pipe1.mediums[1].phase, 0)) ($RES_SIM_264)
(34)      [SCAL] (1) $FUN_11 = semiLinear(pipe3.port_a.m_flow, splitter.port_3.h_outflow, pipe3.mediums[1].h) ($RES_$AUX_421)
(35)      [SCAL] (1) pipe1.state_a.d = Modelica.Media.Water.IF97_Utilities.rho_ph(pipe1.port_a.p, source.ports[1].h_outflow, 0, 0) ($RES_SIM_439)
(36)      [SCAL] (1) pipe1.mediums[1].d = Modelica.Media.Water.IF97_Utilities.rho_props_ph(pipe1.mediums[1].p, pipe1.mediums[1].h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(pipe1.mediums[1].p, pipe1.mediums[1].h, pipe1.mediums[1].phase, 0)) ($RES_SIM_265)
(37)      [FOR-] (2) ($RES_BND_390)
(37)      [----] for $i1 in 1:2 loop
(37)      [----]   [SCAL] (1) pipe3.flowModel.mus[$i1] = Modelica.Media.Water.IF97_Utilities.dynamicViscosity(pipe3.flowModel.states.d, pipe3.flowModel.states.h, pipe3.flowModel.states.phase, pipe3.flowModel.states.p) ($RES_BND_391)
(37)      [----] end for;
(38)      [SCAL] (1) $FUN_12 = semiLinear(valveIncompressible1.port_b.m_flow, valveIncompressible1.port_a.h_outflow, pipe3.mediums[1].h) ($RES_$AUX_420)
(39)      [SCAL] (1) pipe1.mediums[1].phase = if $SEV_40 then 1 else 2 ($RES_SIM_266)
(40)      [ARRY] (1) pipe3.flowModel.pathLengths_internal = pipe3.flowModel.pathLengths ($RES_BND_392)
(41)      [SCAL] (1) source.ports[1].p = source.p ($RES_SIM_268)
(42)      [SCAL] (1) pipe3.flowModel.Res_turbulent_internal[1] = pipe3.flowModel.Re_turbulent ($RES_BND_393)
(43)      [SCAL] (1) source.ports[1].h_outflow = source.medium.h ($RES_SIM_269)
(44)      [ARRY] (1) pipe3.flowModel.diameters = 0.5 * (pipe3.flowModel.dimensions[2:2] + pipe3.flowModel.dimensions[1:1]) ($RES_BND_394)
(45)      [ARRY] (1) pipe3.vs = {(0.5 * (pipe3.m_flows[2] + pipe3.m_flows[1])) / (pipe3.crossAreas[1] * pipe3.mediums[1].d)} / pipe3.nParallel ($RES_BND_396)
(46)      [ARRY] (1) pipe3.heatTransfer.Ts = {pipe3.heatTransfer.states.h} ($RES_BND_398)
(47)      [ARRY] (1) pipe3.heatTransfer.vs = pipe3.vs ($RES_BND_399)
(48)      [SCAL] (1) sink.medium.h = sink.medium.state.h ($RES_SIM_181)
(49)      [SCAL] (1) sink.medium.u = sink.medium.h - sink.p / sink.medium.d ($RES_SIM_183)
(50)      [SCAL] (1) sink.medium.sat.psat = sink.p ($RES_SIM_184)
(51)      [SCAL] (1) -((-273.15) - sink.medium.T_degC) = Modelica.Media.Water.IF97_Utilities.T_props_ph(sink.p, sink.medium.h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(sink.p, sink.medium.h, sink.medium.phase, 0)) ($RES_SIM_186)
(52)      [SCAL] (1) sink.medium.d = Modelica.Media.Water.IF97_Utilities.rho_props_ph(sink.p, sink.medium.h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(sink.p, sink.medium.h, sink.medium.phase, 0)) ($RES_SIM_187)
(53)      [SCAL] (1) sink.medium.phase = if $SEV_24 then 1 else 2 ($RES_SIM_188)
(54)      [SCAL] (1) pipe1.state_a.T = Modelica.Media.Water.IF97_Utilities.T_ph(pipe1.port_a.p, source.ports[1].h_outflow, 0, 0) ($RES_SIM_440)
(55)      [TUPL] (4) ($FUN_13, $FUN_14, $FUN_15, $FUN_16) = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveOpening1.getInterpolationCoefficients(valveOpening1.table, valveOpening1.offset, valveOpening1.startTime, time, valveOpening1.last, 1e-13, valveOpening1.shiftTime) ($RES_$AUX_419)
(56)      [SCAL] (1) pipe1.state_a.p = pipe1.port_a.p ($RES_SIM_441)
(57)      [TUPL] (4) ($FUN_17, $FUN_18, $FUN_19, $FUN_20) = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.valveOpening2.getInterpolationCoefficients(valveOpening2.table, valveOpening2.offset, valveOpening2.startTime, time, valveOpening2.last, 1e-13, valveOpening2.shiftTime) ($RES_$AUX_418)
(58)      [SCAL] (1) pipe1.state_b.phase = 0 ($RES_SIM_442)
(59)      [SCAL] (1) $FUN_21 = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.pipe3.flowModel.WallFriction.pressureLoss_m_flow(pipe3.flowModel.m_flow_nominal / pipe3.flowModel.nParallel, pipe3.flowModel.rho_nominal, pipe3.flowModel.rho_nominal, pipe3.flowModel.mu_nominal, pipe3.flowModel.mu_nominal, pipe3.flowModel.pathLengths_internal[1], pipe3.flowModel.diameters[1], (0.5 .* (pipe3.flowModel.crossAreas[2:2] + pipe3.flowModel.crossAreas[1:1]))[1], (0.5 .* (pipe3.flowModel.roughnesses[2:2] + pipe3.flowModel.roughnesses[1:1]))[1], pipe3.flowModel.m_flow_small / pipe3.flowModel.nParallel, pipe3.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_417)
(60)      [SCAL] (1) pipe1.state_b.h = splitter.port_3.h_outflow ($RES_SIM_443)
(61)      [SCAL] (1) pipe3.flowModel.dp_fric_nominal = sum({$FUN_21}) ($RES_$AUX_416)
(62)      [SCAL] (1) pipe1.state_b.d = Modelica.Media.Water.IF97_Utilities.rho_ph(99999.99999999999 * splitter.medium.p_bar, splitter.port_3.h_outflow, 0, 0) ($RES_SIM_444)
(63)      [SCAL] (1) source.medium.h = Modelica.Media.Water.IF97_Utilities.h_pT(source.p, source.T, 0) ($RES_SIM_270)
(64)      [SCAL] (1) $FUN_23 = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.pipe2.flowModel.WallFriction.pressureLoss_m_flow(pipe2.flowModel.m_flow_nominal / pipe2.flowModel.nParallel, pipe2.flowModel.rho_nominal, pipe2.flowModel.rho_nominal, pipe2.flowModel.mu_nominal, pipe2.flowModel.mu_nominal, pipe2.flowModel.pathLengths_internal[1], pipe2.flowModel.diameters[1], (0.5 .* (pipe2.flowModel.crossAreas[2:2] + pipe2.flowModel.crossAreas[1:1]))[1], (0.5 .* (pipe2.flowModel.roughnesses[2:2] + pipe2.flowModel.roughnesses[1:1]))[1], pipe2.flowModel.m_flow_small / pipe2.flowModel.nParallel, pipe2.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_415)
(65)      [SCAL] (1) pipe1.state_b.T = Modelica.Media.Water.IF97_Utilities.T_ph(99999.99999999999 * splitter.medium.p_bar, splitter.port_3.h_outflow, 0, 0) ($RES_SIM_445)
(66)      [SCAL] (1) pipe2.flowModel.dp_fric_nominal = sum({$FUN_23}) ($RES_$AUX_414)
(67)      [SCAL] (1) pipe1.state_b.p = 99999.99999999999 * splitter.medium.p_bar ($RES_SIM_446)
(68)      [SCAL] (1) $FUN_25 = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes4.pipe1.flowModel.WallFriction.pressureLoss_m_flow(pipe1.flowModel.m_flow_nominal / pipe1.flowModel.nParallel, pipe1.flowModel.rho_nominal, pipe1.flowModel.rho_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.pathLengths_internal[$i1], pipe1.flowModel.diameters[$i1], (0.5 .* (pipe1.flowModel.crossAreas[2:3] + pipe1.flowModel.crossAreas[1:2]))[$i1], (0.5 .* (pipe1.flowModel.roughnesses[2:3] + pipe1.flowModel.roughnesses[1:2]))[$i1], pipe1.flowModel.m_flow_small / pipe1.flowModel.nParallel, pipe1.flowModel.Res_turbulent_internal[$i1]) ($RES_$AUX_413)
(69)      [SCAL] (1) valveIncompressible.state_a.phase = 0 ($RES_SIM_447)
(70)      [SCAL] (1) pipe1.flowModel.dp_fric_nominal = sum($FUN_25 for $i1 in 1:2) ($RES_$AUX_412)
(71)      [SCAL] (1) valveIncompressible.state_a.h = valveIncompressible.port_b.h_outflow ($RES_SIM_448)
(72)      [SCAL] (1) valveIncompressible.state_a.d = Modelica.Media.Water.IF97_Utilities.rho_ph(pipe2.port_b.p, valveIncompressible.port_b.h_outflow, 0, 0) ($RES_SIM_449)
(73)      [SCAL] (1) valveIncompressible1.dp = pipe3.port_b.p - valveIncompressible1.port_b.p ($RES_SIM_192)
(74)      [SCAL] (1) valveIncompressible1.port_a.h_outflow = sink.ports[2].h_outflow ($RES_SIM_196)
(75)      [SCAL] (1) -valveIncompressible1.port_b.m_flow = homotopy(valveIncompressible1.Av * valveIncompressible1.relativeFlowCoefficient * smooth(2, if $SEV_25 then (if $SEV_26 then sqrt(valveIncompressible1.state_a.d) else 0.0) * sqrt(valveIncompressible1.dp) else if $SEV_27 then -(if $SEV_28 then sqrt(valveIncompressible1.state_b.d) else 0.0) * sqrt(abs(valveIncompressible1.dp)) else if $SEV_29 then Modelica.Fluid.Utilities.regRoot2.regRoot2_utility(valveIncompressible1.dp, valveIncompressible1.dp_turbulent, valveIncompressible1.state_a.d, valveIncompressible1.state_b.d, false, 1.0) else -Modelica.Fluid.Utilities.regRoot2.regRoot2_utility(-valveIncompressible1.dp, valveIncompressible1.dp_turbulent, valveIncompressible1.state_b.d, valveIncompressible1.state_a.d, false, 1.0)), (valveIncompressible1.dp * valveIncompressible1.m_flow_nominal * valveIncompressible1.relativeFlowCoefficient) / valveIncompressible1.dp_nominal) ($RES_SIM_197)
(76)      [SCAL] (1) valveIncompressible1.minLimiter.y = smooth(0, noEvent(if $SEV_30 then valveIncompressible1.minLimiter.uMin else valveIncompressible1.relativeFlowCoefficient)) ($RES_SIM_199)
(77)      [SCAL] (1) valveIncompressible.state_a.T = Modelica.Media.Water.IF97_Utilities.T_ph(pipe2.port_b.p, valveIncompressible.port_b.h_outflow, 0, 0) ($RES_SIM_450)
(78)      [SCAL] (1) valveIncompressible.state_a.p = pipe2.port_b.p ($RES_SIM_451)
(79)      [SCAL] (1) valveIncompressible.state_b.phase = 0 ($RES_SIM_452)
(80)      [SCAL] (1) $TEV_0 = $PRE.valveOpening2.nextEvent ($RES_EVT_497)
(81)      [SCAL] (1) valveIncompressible.state_b.h = sink.ports[1].h_outflow ($RES_SIM_453)
(82)      [SCAL] (1) $TEV_1 = $PRE.valveOpening1.nextEvent ($RES_EVT_498)
(83)      [SCAL] (1) valveIncompressible.state_b.d = Modelica.Media.Water.IF97_Utilities.rho_ph(valveIncompressible.port_b.p, sink.ports[1].h_outflow, 0, 0) ($RES_SIM_454)
(84)      [SCAL] (1) $SEV_8 = (-pipe2.port_a.m_flow) > 0.0 ($RES_EVT_499)
(85)      [SCAL] (1) source.medium.phase = source.medium.state.phase ($RES_SIM_280)
(86)      [SCAL] (1) valveIncompressible.state_b.T = Modelica.Media.Water.IF97_Utilities.T_ph(valveIncompressible.port_b.p, sink.ports[1].h_outflow, 0, 0) ($RES_SIM_455)
(87)      [SCAL] (1) source.medium.d = source.medium.state.d ($RES_SIM_281)
(88)      [SCAL] (1) valveIncompressible.state_b.p = valveIncompressible.port_b.p ($RES_SIM_456)
(89)      [SCAL] (1) -((-273.15) - source.medium.T_degC) = source.medium.state.T ($RES_SIM_282)
(90)      [SCAL] (1) valveIncompressible1.state_a.phase = 0 ($RES_SIM_457)
(91)      [SCAL] (1) valveIncompressible1.state_a.h = valveIncompressible1.port_b.h_outflow ($RES_SIM_458)
(92)      [SCAL] (1) source.medium.h = source.medium.state.h ($RES_SIM_284)
(93)      [SCAL] (1) valveIncompressible1.state_a.d = Modelica.Media.Water.IF97_Utilities.rho_ph(pipe3.port_b.p, valveIncompressible1.port_b.h_outflow, 0, 0) ($RES_SIM_459)
(94)      [SCAL] (1) source.medium.u = source.medium.h - source.p / source.medium.d ($RES_SIM_286)
(95)      [SCAL] (1) source.medium.sat.psat = source.p ($RES_SIM_287)
(96)      [SCAL] (1) -((-273.15) - source.medium.T_degC) = Modelica.Media.Water.IF97_Utilities.T_props_ph(source.p, source.medium.h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(source.p, source.medium.h, source.medium.phase, 0)) ($RES_SIM_289)
(97)      [SCAL] (1) valveIncompressible1.state_a.T = Modelica.Media.Water.IF97_Utilities.T_ph(pipe3.port_b.p, valveIncompressible1.port_b.h_outflow, 0, 0) ($RES_SIM_460)
(98)      [SCAL] (1) valveIncompressible1.state_a.p = pipe3.port_b.p ($RES_SIM_461)
(99)      [SCAL] (1) valveIncompressible1.state_b.phase = 0 ($RES_SIM_462)
(100)     [SCAL] (1) valveIncompressible1.state_b.h = sink.ports[2].h_outflow ($RES_SIM_463)
(101)     [SCAL] (1) valveIncompressible1.state_b.d = Modelica.Media.Water.IF97_Utilities.rho_ph(valveIncompressible1.port_b.p, sink.ports[2].h_outflow, 0, 0) ($RES_SIM_464)
(102)     [SCAL] (1) source.medium.d = Modelica.Media.Water.IF97_Utilities.rho_props_ph(source.p, source.medium.h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(source.p, source.medium.h, source.medium.phase, 0)) ($RES_SIM_290)
(103)     [SCAL] (1) valveIncompressible1.state_b.T = Modelica.Media.Water.IF97_Utilities.T_ph(valveIncompressible1.port_b.p, sink.ports[2].h_outflow, 0, 0) ($RES_SIM_465)
(104)     [SCAL] (1) source.medium.phase = if $SEV_43 then 1 else 2 ($RES_SIM_291)
(105)     [SCAL] (1) valveIncompressible1.state_b.p = valveIncompressible1.port_b.p ($RES_SIM_466)
(106)     [SCAL] (1) pipe2.state_a.phase = 0 ($RES_SIM_467)
(107)     [SCAL] (1) pipe2.state_a.h = splitter.port_3.h_outflow ($RES_SIM_468)
(108)     [SCAL] (1) pipe3.heatTransfer.heatPorts[1].Q_flow = 0.0 ($RES_SIM_294)
(109)     [SCAL] (1) pipe2.state_a.d = Modelica.Media.Water.IF97_Utilities.rho_ph(99999.99999999999 * splitter.medium.p_bar, splitter.port_3.h_outflow, 0, 0) ($RES_SIM_469)
(110)     [SCAL] (1) pipe2.heatTransfer.heatPorts[1].Q_flow = 0.0 ($RES_SIM_296)
(111)     [SCAL] (1) sink.ports[2].m_flow + valveIncompressible1.port_b.m_flow = 0.0 ($RES_SIM_299)
(112)     [SCAL] (1) pipe2.state_a.T = Modelica.Media.Water.IF97_Utilities.T_ph(99999.99999999999 * splitter.medium.p_bar, splitter.port_3.h_outflow, 0, 0) ($RES_SIM_470)
(113)     [SCAL] (1) pipe2.state_a.p = 99999.99999999999 * splitter.medium.p_bar ($RES_SIM_471)
(114)     [ALGO] (5) ($RES_SIM_16)
(114)     [----] assert(not (valveOpening2.table[1, 1] > 0.0 or valveOpening2.table[1, 1] < 0.0), "The first point in time has to be set to 0, but is table[1,1] = " + String(valveOpening2.table[1, 1], 6, 0, true), AssertionLevel.error);

(114)     [----] when {time >= $PRE.valveOpening2.nextEvent, initial()} then
(114)     [----]   (valveOpening2.a, valveOpening2.b, valveOpening2.nextEventScaled, valveOpening2.last) := ($FUN_17, $FUN_18, $FUN_19, $FUN_20);
(114)     [----]   valveOpening2.nextEvent := valveOpening2.nextEventScaled;
(114)     [----] end when;

(115)     [ALGO] (5) ($RES_SIM_17)
(115)     [----] assert(not (valveOpening1.table[1, 1] > 0.0 or valveOpening1.table[1, 1] < 0.0), "The first point in time has to be set to 0, but is table[1,1] = " + String(valveOpening1.table[1, 1], 6, 0, true), AssertionLevel.error);

(115)     [----] when {time >= $PRE.valveOpening1.nextEvent, initial()} then
(115)     [----]   (valveOpening1.a, valveOpening1.b, valveOpening1.nextEventScaled, valveOpening1.last) := ($FUN_13, $FUN_14, $FUN_15, $FUN_16);
(115)     [----]   valveOpening1.nextEvent := valveOpening1.nextEventScaled;
(115)     [----] end when;

(116)     [SCAL] (1) pipe2.state_b.h = valveIncompressible.port_a.h_outflow ($RES_SIM_473)
(117)     [SCAL] (1) $DER.splitter.m = splitter.mb_flow ($RES_SIM_18)
(118)     [SCAL] (1) pipe2.state_b.d = Modelica.Media.Water.IF97_Utilities.rho_ph(pipe2.port_b.p, valveIncompressible.port_a.h_outflow, 0, 0) ($RES_SIM_474)
(119)     [SCAL] (1) $DER.splitter.U = splitter.Hb_flow ($RES_SIM_19)
(120)     [SCAL] (1) pipe2.state_b.T = Modelica.Media.Water.IF97_Utilities.T_ph(pipe2.port_b.p, valveIncompressible.port_a.h_outflow, 0, 0) ($RES_SIM_475)
(121)     [SCAL] (1) pipe2.state_b.p = pipe2.port_b.p ($RES_SIM_476)
(122)     [SCAL] (1) pipe3.state_a.phase = 0 ($RES_SIM_477)
(123)     [SCAL] (1) pipe3.state_a.h = splitter.port_3.h_outflow ($RES_SIM_478)
(124)     [SCAL] (1) pipe3.state_a.d = Modelica.Media.Water.IF97_Utilities.rho_ph(99999.99999999999 * splitter.medium.p_bar, splitter.port_3.h_outflow, 0, 0) ($RES_SIM_479)
(125)     [SCAL] (1) splitter.U = splitter.m * splitter.medium.u ($RES_SIM_20)
(126)     [SCAL] (1) splitter.m = splitter.V * splitter.medium.d ($RES_SIM_21)
(127)     [SCAL] (1) splitter.Hb_flow = smooth(0, -pipe2.port_a.m_flow * (if $SEV_8 then pipe2.port_a.h_outflow else splitter.port_3.h_outflow)) + smooth(0, -pipe3.port_a.m_flow * (if $SEV_9 then pipe3.port_a.h_outflow else splitter.port_3.h_outflow)) + smooth(0, -pipe1.port_b.m_flow * (if $SEV_10 then pipe1.port_b.h_outflow else splitter.port_3.h_outflow)) ($RES_SIM_24)
(128)     [SCAL] (1) pipe3.state_a.T = Modelica.Media.Water.IF97_Utilities.T_ph(99999.99999999999 * splitter.medium.p_bar, splitter.port_3.h_outflow, 0, 0) ($RES_SIM_480)
(129)     [SCAL] (1) pipe3.state_a.p = 99999.99999999999 * splitter.medium.p_bar ($RES_SIM_481)
(130)     [SCAL] (1) pipe3.state_b.h = valveIncompressible1.port_a.h_outflow ($RES_SIM_483)
(131)     [SCAL] (1) splitter.mb_flow = -(pipe2.port_a.m_flow + pipe3.port_a.m_flow + pipe1.port_b.m_flow) ($RES_SIM_28)
(132)     [SCAL] (1) pipe3.state_b.d = Modelica.Media.Water.IF97_Utilities.rho_ph(pipe3.port_b.p, valveIncompressible1.port_a.h_outflow, 0, 0) ($RES_SIM_484)
(133)     [SCAL] (1) pipe3.state_b.T = Modelica.Media.Water.IF97_Utilities.T_ph(pipe3.port_b.p, valveIncompressible1.port_a.h_outflow, 0, 0) ($RES_SIM_485)
(134)     [SCAL] (1) pipe3.state_b.p = pipe3.port_b.p ($RES_SIM_486)
(135)     [SCAL] (1) splitter.medium.phase = splitter.medium.state.phase ($RES_SIM_36)
(136)     [SCAL] (1) splitter.medium.d = splitter.medium.state.d ($RES_SIM_37)
(137)     [SCAL] (1) -((-273.15) - splitter.medium.T_degC) = splitter.medium.state.T ($RES_SIM_38)
(138)     [SCAL] (1) 99999.99999999999 * splitter.medium.p_bar = splitter.medium.state.p ($RES_SIM_39)
(139)     [SCAL] (1) splitter.port_3.h_outflow = splitter.medium.state.h ($RES_SIM_40)
(140)     [SCAL] (1) splitter.medium.u = splitter.port_3.h_outflow - (99999.99999999999 * splitter.medium.p_bar) / splitter.medium.d ($RES_SIM_42)
(141)     [SCAL] (1) splitter.medium.sat.psat = 99999.99999999999 * splitter.medium.p_bar ($RES_SIM_43)
(142)     [SCAL] (1) splitter.medium.sat.Tsat = Modelica.Media.Water.IF97_Utilities.BaseIF97.Basic.tsat(99999.99999999999 * splitter.medium.p_bar) ($RES_SIM_44)
(143)     [SCAL] (1) -((-273.15) - splitter.medium.T_degC) = Modelica.Media.Water.IF97_Utilities.T_props_ph(99999.99999999999 * splitter.medium.p_bar, splitter.port_3.h_outflow, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(99999.99999999999 * splitter.medium.p_bar, splitter.port_3.h_outflow, splitter.medium.phase, 0)) ($RES_SIM_45)
(144)     [SCAL] (1) splitter.medium.d = Modelica.Media.Water.IF97_Utilities.rho_props_ph(99999.99999999999 * splitter.medium.p_bar, splitter.port_3.h_outflow, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(99999.99999999999 * splitter.medium.p_bar, splitter.port_3.h_outflow, splitter.medium.phase, 0)) ($RES_SIM_46)
(145)     [SCAL] (1) splitter.medium.phase = if $SEV_13 then 1 else 2 ($RES_SIM_47)
(146)     [SCAL] (1) valveIncompressible1.relativeFlowCoefficient = valveOpening2.a * time + valveOpening2.b ($RES_SIM_49)
(147)     [SCAL] (1) valveIncompressible.relativeFlowCoefficient = valveOpening1.a * time + valveOpening1.b ($RES_SIM_51)
(148)     [SCAL] (1) $DER.pipe3.ms[1] = pipe3.mb_flows[1] ($RES_SIM_53)
(149)     [SCAL] (1) $DER.pipe3.Us[1] = pipe3.Wb_flows[1] + pipe3.Hb_flows[1] + pipe3.Qb_flows[1] ($RES_SIM_54)
(150)     [SCAL] (1) pipe3.ms[1] = pipe3.fluidVolumes[1] * pipe3.mediums[1].d ($RES_SIM_55)
(151)     [SCAL] (1) pipe3.Us[1] = pipe3.ms[1] * pipe3.mediums[1].u ($RES_SIM_56)
(152)     [SCAL] (1) pipe3.port_b.p = pipe3.mediums[1].p ($RES_SIM_57)
(153)     [ARRY] (1) pipe3.vsFM[2:2] = pipe3.vs ($RES_SIM_58)
(154)     [SCAL] (1) pipe3.vsFM[1] = ((pipe3.m_flows[1] / pipe3.state_a.d) / pipe3.crossAreas[1]) / pipe3.nParallel ($RES_SIM_59)
(155)     [SCAL] (1) pipe3.mediums[1].u = pipe3.mediums[1].h - pipe3.mediums[1].p / pipe3.mediums[1].d ($RES_SIM_101)
(156)     [ARRY] (1) pipe3.mediums.sat.psat = pipe3.mediums.p ($RES_SIM_102)
(157)     [SCAL] (1) pipe3.mediums[1].sat.Tsat = Modelica.Media.Water.IF97_Utilities.BaseIF97.Basic.tsat(pipe3.mediums[1].p) ($RES_SIM_103)
(158)     [SCAL] (1) pipe3.mediums[1].T = Modelica.Media.Water.IF97_Utilities.T_props_ph(pipe3.mediums[1].p, pipe3.mediums[1].h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(pipe3.mediums[1].p, pipe3.mediums[1].h, pipe3.mediums[1].phase, 0)) ($RES_SIM_104)
(159)     [SCAL] (1) pipe3.mediums[1].d = Modelica.Media.Water.IF97_Utilities.rho_props_ph(pipe3.mediums[1].p, pipe3.mediums[1].h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(pipe3.mediums[1].p, pipe3.mediums[1].h, pipe3.mediums[1].phase, 0)) ($RES_SIM_105)
(160)     [SCAL] (1) pipe3.mediums[1].phase = if $SEV_17 then 1 else 2 ($RES_SIM_106)
(161)     [ARRY] (15) pipe1.flowModel.states = pipe1.statesFM ($RES_BND_406)
(162)     [ARRY] (5) pipe1.heatTransfer.states = pipe1.mediums.state ($RES_BND_407)
(163)     [SCAL] (1) $DER.pipe2.ms[1] = pipe2.mb_flows[1] ($RES_SIM_108)
(164)     [ARRY] (10) pipe2.flowModel.states = pipe2.statesFM ($RES_BND_408)
(165)     [SCAL] (1) $DER.pipe2.Us[1] = pipe2.Wb_flows[1] + pipe2.Hb_flows[1] + pipe2.Qb_flows[1] ($RES_SIM_109)
(166)     [ARRY] (5) pipe2.heatTransfer.states = pipe2.mediums.state ($RES_BND_409)
(167)     [ARRY] (1) pipe3.m_flows[1:1] = pipe3.flowModel.m_flows[:] ($RES_SIM_60)
(168)     [ARRY] (5) pipe3.statesFM[2:2] = pipe3.mediums[:].state ($RES_SIM_61)
(169)     [RECD] (5) pipe3.statesFM[1] = pipe3.state_a ($RES_SIM_62)
(170)     [SCAL] (1) valveIncompressible1.port_b.h_outflow = pipe3.mediums[1].h ($RES_SIM_65)
(171)     [SCAL] (1) pipe3.port_a.h_outflow = pipe3.mediums[1].h ($RES_SIM_66)
(172)     [SCAL] (1) valveIncompressible1.port_b.m_flow = -pipe3.m_flows[2] ($RES_SIM_67)
(173)     [ARRY] (1) pipe1.fluidVolumes = {10.0 * pipe1.crossAreas[1]} .* pipe1.nParallel ($RES_BND_320)
(174)     [SCAL] (1) pipe3.port_a.m_flow = pipe3.m_flows[1] ($RES_SIM_68)
(175)     [ARRY] (1) pipe1.mediums.p_bar = {1e-5 * pipe1.mediums[1].p} ($RES_BND_321)
(176)     [ARRY] (1) pipe1.mediums.T_degC = {(-273.15) + pipe1.mediums[1].T} ($RES_BND_322)
(177)     [SCAL] (1) pipe3.H_flows[2] = -$FUN_12 ($RES_SIM_69)
(178)     [ARRY] (3) pipe1.flowModel.vs = pipe1.vsFM ($RES_BND_323)
(179)     [ARRY] (3) pipe1.flowModel.crossAreas = pipe1.crossAreasFM ($RES_BND_324)
(180)     [ARRY] (3) pipe1.flowModel.dimensions = pipe1.dimensionsFM ($RES_BND_325)
(181)     [ARRY] (3) pipe1.flowModel.roughnesses = pipe1.roughnessesFM ($RES_BND_326)
(182)     [ARRY] (2) pipe1.flowModel.dheights = pipe1.dheightsFM ($RES_BND_327)
(183)     [ARRY] (2) pipe1.flowModel.pathLengths = pipe1.pathLengths ($RES_BND_328)
(184)     [FOR-] (3) ($RES_BND_329)
(184)     [----] for $i1 in 1:3 loop
(184)     [----]   [SCAL] (1) pipe1.flowModel.rhos[$i1] = pipe1.flowModel.states.d ($RES_BND_330)
(184)     [----] end for;
(185)     [SCAL] (1) pipe2.ms[1] = pipe2.fluidVolumes[1] * pipe2.mediums[1].d ($RES_SIM_110)
(186)     [ARRY] (10) pipe3.flowModel.states = pipe3.statesFM ($RES_BND_410)
(187)     [SCAL] (1) pipe2.Us[1] = pipe2.ms[1] * pipe2.mediums[1].u ($RES_SIM_111)
(188)     [ARRY] (5) pipe3.heatTransfer.states = pipe3.mediums.state ($RES_BND_411)
(189)     [SCAL] (1) pipe2.port_b.p = pipe2.mediums[1].p ($RES_SIM_112)
(190)     [ARRY] (1) pipe2.vsFM[2:2] = pipe2.vs ($RES_SIM_113)
(191)     [SCAL] (1) pipe2.vsFM[1] = ((pipe2.m_flows[1] / pipe2.state_a.d) / pipe2.crossAreas[1]) / pipe2.nParallel ($RES_SIM_114)
(192)     [ARRY] (1) pipe2.m_flows[1:1] = pipe2.flowModel.m_flows[:] ($RES_SIM_115)
(193)     [ARRY] (5) pipe2.statesFM[2:2] = pipe2.mediums[:].state ($RES_SIM_116)
(194)     [RECD] (5) pipe2.statesFM[1] = pipe2.state_a ($RES_SIM_117)
(195)     [SCAL] (1) pipe3.H_flows[1] = $FUN_11 ($RES_SIM_70)
(196)     [SCAL] (1) pipe3.mb_flows[1] = pipe3.m_flows[1] - pipe3.m_flows[2] ($RES_SIM_71)
(197)     [SCAL] (1) pipe3.Hb_flows[1] = pipe3.H_flows[1] - pipe3.H_flows[2] ($RES_SIM_72)
(198)     [ARRY] (2) pipe3.roughnessesFM[:] = {pipe3.roughnesses[1], pipe3.roughnesses[1]} ($RES_SIM_73)
(199)     [SCAL] (1) valveIncompressible.dp = pipe2.port_b.p - valveIncompressible.port_b.p ($RES_SIM_202)
(200)     [ARRY] (2) pipe3.dimensionsFM[:] = {pipe3.dimensions[1], pipe3.dimensions[1]} ($RES_SIM_74)
(201)     [ARRY] (2) pipe3.crossAreasFM[:] = {pipe3.crossAreas[1], pipe3.crossAreas[1]} ($RES_SIM_75)
(202)     [ARRY] (1) pipe3.dheightsFM[:] = {0.0} ($RES_SIM_76)
(203)     [SCAL] (1) $SEV_9 = (-pipe3.port_a.m_flow) > 0.0 ($RES_EVT_500)
(204)     [ARRY] (1) pipe3.pathLengths[:] = {10.0} ($RES_SIM_77)
(205)     [SCAL] (1) $SEV_10 = (-pipe1.port_b.m_flow) > 0.0 ($RES_EVT_501)
(206)     [FOR-] (3) ($RES_BND_331)
(206)     [----] for $i1 in 1:3 loop
(206)     [----]   [SCAL] (1) pipe1.flowModel.mus[$i1] = Modelica.Media.Water.IF97_Utilities.dynamicViscosity(pipe1.flowModel.states.d, pipe1.flowModel.states.h, pipe1.flowModel.states.phase, pipe1.flowModel.states.p) ($RES_BND_332)
(206)     [----] end for;
(207)     [ARRY] (1) pipe3.Wb_flows = (pipe3.crossAreas * pipe3.vs * (($FUN_10 + pipe3.port_b.p) - ((system.g * {0.0}) / pipe3.mediums.d + 99999.99999999999 * splitter.medium.p_bar))) / ({1.0} * {1.0}) .* {1.0} .* pipe3.nParallel ($RES_SIM_78)
(208)     [SCAL] (1) valveIncompressible.port_a.h_outflow = sink.ports[1].h_outflow ($RES_SIM_206)
(209)     [ARRY] (1) pipe3.Qb_flows = pipe3.heatTransfer.Q_flows ($RES_SIM_79)
(210)     [SCAL] (1) -valveIncompressible.port_b.m_flow = homotopy(valveIncompressible.Av * valveIncompressible.relativeFlowCoefficient * smooth(2, if $SEV_31 then (if $SEV_32 then sqrt(valveIncompressible.state_a.d) else 0.0) * sqrt(valveIncompressible.dp) else if $SEV_33 then -(if $SEV_34 then sqrt(valveIncompressible.state_b.d) else 0.0) * sqrt(abs(valveIncompressible.dp)) else if $SEV_35 then Modelica.Fluid.Utilities.regRoot2.regRoot2_utility(valveIncompressible.dp, valveIncompressible.dp_turbulent, valveIncompressible.state_a.d, valveIncompressible.state_b.d, false, 1.0) else -Modelica.Fluid.Utilities.regRoot2.regRoot2_utility(-valveIncompressible.dp, valveIncompressible.dp_turbulent, valveIncompressible.state_b.d, valveIncompressible.state_a.d, false, 1.0)), (valveIncompressible.dp * valveIncompressible.m_flow_nominal * valveIncompressible.relativeFlowCoefficient) / valveIncompressible.dp_nominal) ($RES_SIM_207)
(211)     [ARRY] (2) pipe1.flowModel.pathLengths_internal = pipe1.flowModel.pathLengths ($RES_BND_333)
(212)     [SCAL] (1) $SEV_13 = (splitter.port_3.h_outflow < Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(splitter.medium.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(splitter.medium.sat.psat)) or splitter.port_3.h_outflow > Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(splitter.medium.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(splitter.medium.sat.psat))) or 99999.99999999999 * splitter.medium.p_bar > 2.2064e7 ($RES_EVT_504)
(213)     [FOR-] (2) ($RES_BND_334)
(213)     [----] for $i1 in 1:2 loop
(213)     [----]   [SCAL] (1) pipe1.flowModel.Res_turbulent_internal[$i1] = pipe1.flowModel.Re_turbulent ($RES_BND_335)
(213)     [----] end for;
(214)     [SCAL] (1) valveIncompressible.minLimiter.y = smooth(0, noEvent(if $SEV_36 then valveIncompressible.minLimiter.uMin else valveIncompressible.relativeFlowCoefficient)) ($RES_SIM_209)
(215)     [SCAL] (1) $SEV_14 = pipe3.flowModel.m_flows[1] > 0.0 ($RES_EVT_505)
(216)     [SCAL] (1) $SEV_15[1] = pipe3.mediums[1].p >= 0.0 ($RES_EVT_506)
(217)     [ARRY] (2) pipe1.flowModel.diameters = 0.5 * (pipe1.flowModel.dimensions[2:3] + pipe1.flowModel.dimensions[1:2]) ($RES_BND_336)
(218)     [SCAL] (1) $SEV_17 = (pipe3.mediums[1].h < Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(pipe3.mediums.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(pipe3.mediums.sat.psat)) or pipe3.mediums[1].h > Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(pipe3.mediums.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(pipe3.mediums.sat.psat))) or pipe3.mediums[1].p > 2.2064e7 ($RES_EVT_508)
(219)     [ARRY] (1) pipe1.vs = {(0.5 * (pipe1.m_flows[2] + pipe1.m_flows[1])) / (pipe1.crossAreas[1] * pipe1.mediums[1].d)} / pipe1.nParallel ($RES_BND_338)
(220)     [SCAL] (1) $SEV_18 = pipe2.flowModel.m_flows[1] > 0.0 ($RES_EVT_509)
(221)     [SCAL] (1) valveIncompressible.port_b.h_outflow = pipe2.mediums[1].h ($RES_SIM_120)
(222)     [SCAL] (1) pipe2.port_a.h_outflow = pipe2.mediums[1].h ($RES_SIM_121)
(223)     [SCAL] (1) valveIncompressible.port_b.m_flow = -pipe2.m_flows[2] ($RES_SIM_122)
(224)     [SCAL] (1) pipe2.port_a.m_flow = pipe2.m_flows[1] ($RES_SIM_123)
(225)     [SCAL] (1) pipe2.H_flows[2] = -$FUN_8 ($RES_SIM_124)
(226)     [SCAL] (1) pipe2.H_flows[1] = $FUN_7 ($RES_SIM_125)
(227)     [SCAL] (1) pipe2.mb_flows[1] = pipe2.m_flows[1] - pipe2.m_flows[2] ($RES_SIM_126)
(228)     [SCAL] (1) pipe2.Hb_flows[1] = pipe2.H_flows[1] - pipe2.H_flows[2] ($RES_SIM_127)
(229)     [ARRY] (2) pipe2.roughnessesFM[:] = {pipe2.roughnesses[1], pipe2.roughnesses[1]} ($RES_SIM_128)
(230)     [ARRY] (2) pipe2.dimensionsFM[:] = {pipe2.dimensions[1], pipe2.dimensions[1]} ($RES_SIM_129)
(231)     [ARRY] (1) pipe3.heatTransfer.Q_flows = pipe3.heatTransfer.heatPorts.Q_flow ($RES_SIM_80)
(232)     [ARRY] (1) pipe3.heatTransfer.Ts = pipe3.heatTransfer.heatPorts.T ($RES_SIM_81)
(233)     [SCAL] (1) $DER.pipe1.ms[1] = pipe1.mb_flows[1] ($RES_SIM_210)
(234)     [ARRY] (1) {0.0} = pipe3.flowModel.Ib_flows - (pipe3.flowModel.Fs_fg + pipe3.flowModel.Fs_p) ($RES_SIM_82)
(235)     [SCAL] (1) $DER.pipe1.Us[1] = pipe1.Wb_flows[1] + pipe1.Hb_flows[1] + pipe1.Qb_flows[1] ($RES_SIM_211)
(236)     [ARRY] (1) pipe3.flowModel.Is = {pipe3.flowModel.m_flows[1] * pipe3.flowModel.pathLengths[1]} ($RES_SIM_83)
(237)     [SCAL] (1) pipe1.ms[1] = pipe1.fluidVolumes[1] * pipe1.mediums[1].d ($RES_SIM_212)
(238)     [ARRY] (1) pipe3.flowModel.dps_fg = {(2.0 * (pipe3.flowModel.Fs_fg[1] / pipe3.flowModel.nParallel)) / (pipe3.flowModel.crossAreas[1] + pipe3.flowModel.crossAreas[2])} ($RES_SIM_84)
(239)     [SCAL] (1) pipe1.Us[1] = pipe1.ms[1] * pipe1.mediums[1].u ($RES_SIM_213)
(240)     [ARRY] (1) pipe3.flowModel.Fs_p = pipe3.flowModel.nParallel * {0.5 * (pipe3.flowModel.crossAreas[1] + pipe3.flowModel.crossAreas[2]) * (pipe3.flowModel.states.phase - pipe3.flowModel.states.phase)} ($RES_SIM_85)
(241)     [SCAL] (1) pipe1.vsFM[3] = ((pipe1.m_flows[2] / pipe1.state_b.d) / pipe1.crossAreas[1]) / pipe1.nParallel ($RES_SIM_214)
(242)     [ARRY] (1) pipe3.flowModel.Ib_flows = {0.0} ($RES_SIM_86)
(243)     [SCAL] (1) $SEV_19[1] = pipe2.mediums[1].p >= 0.0 ($RES_EVT_510)
(244)     [ARRY] (1) pipe1.vsFM[2:2] = pipe1.vs ($RES_SIM_215)
(245)     [ARRY] (1) pipe1.heatTransfer.Ts = {pipe1.heatTransfer.states.h} ($RES_BND_340)
(246)     [SCAL] (1) pipe3.flowModel.rhos_act[1] = noEvent(if $SEV_14 then pipe3.flowModel.rhos[1] else pipe3.flowModel.rhos[2]) ($RES_SIM_87)
(247)     [SCAL] (1) pipe1.vsFM[1] = ((pipe1.m_flows[1] / pipe1.state_a.d) / pipe1.crossAreas[1]) / pipe1.nParallel ($RES_SIM_216)
(248)     [ARRY] (1) pipe1.heatTransfer.vs = pipe1.vs ($RES_BND_341)
(249)     [SCAL] (1) pipe3.flowModel.mus_act[1] = noEvent(if $SEV_14 then pipe3.flowModel.mus[1] else pipe3.flowModel.mus[2]) ($RES_SIM_88)
(250)     [SCAL] (1) $SEV_21 = (pipe2.mediums[1].h < Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(pipe2.mediums.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(pipe2.mediums.sat.psat)) or pipe2.mediums[1].h > Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(pipe2.mediums.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(pipe2.mediums.sat.psat))) or pipe2.mediums[1].p > 2.2064e7 ($RES_EVT_512)
(251)     [ARRY] (2) pipe1.m_flows[:] = pipe1.flowModel.m_flows[:] ($RES_SIM_217)
(252)     [ARRY] (1) pipe3.flowModel.m_flows = {homotopy(({$FUN_9} .* pipe3.flowModel.nParallel)[1], (pipe3.flowModel.m_flow_nominal / pipe3.flowModel.dp_nominal * (pipe3.flowModel.dps_fg - (pipe3.flowModel.g * pipe3.flowModel.dheights) .* pipe3.flowModel.rho_nominal))[1])} ($RES_SIM_89)
(253)     [RECD] (5) pipe1.statesFM[3] = pipe1.state_b ($RES_SIM_218)
(254)     [ARRY] (5) pipe1.statesFM[2:2] = pipe1.mediums[:].state ($RES_SIM_219)
(255)     [SCAL] (1) $SEV_24 = (sink.medium.h < Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(sink.medium.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(sink.medium.sat.psat)) or sink.medium.h > Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(sink.medium.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(sink.medium.sat.psat))) or sink.p > 2.2064e7 ($RES_EVT_515)
(256)     [SCAL] (1) valveIncompressible.V_flow = -valveIncompressible.port_b.m_flow / smooth(1, if $SEV_52 then valveIncompressible.state_a.d else if $SEV_53 then valveIncompressible.state_b.d else if $SEV_51 then 0.5 * (valveIncompressible.state_a.d + valveIncompressible.state_b.d) - 0.25 * (valveIncompressible.state_b.d - valveIncompressible.state_a.d) * ((-3.0) + (valveIncompressible.port_b.m_flow / (-valveIncompressible.m_flow_small)) ^ 2.0) * (valveIncompressible.port_b.m_flow / valveIncompressible.m_flow_small) else 0.5 * (valveIncompressible.state_a.d + valveIncompressible.state_b.d)) ($RES_BND_345)
(257)     [SCAL] (1) $SEV_25 = valveIncompressible1.dp >= valveIncompressible1.dp_turbulent ($RES_EVT_516)
(258)     [SCAL] (1) valveIncompressible.port_a_T = smooth(1, if $SEV_52 then valveIncompressible.state_a.T else if $SEV_53 then Modelica.Media.Water.IF97_Utilities.T_ph(pipe2.port_b.p, valveIncompressible.port_a.h_outflow, 0, 0) else if $SEV_51 then 0.5 * (valveIncompressible.state_a.T + Modelica.Media.Water.IF97_Utilities.T_ph(pipe2.port_b.p, valveIncompressible.port_a.h_outflow, 0, 0)) - 0.25 * (Modelica.Media.Water.IF97_Utilities.T_ph(pipe2.port_b.p, valveIncompressible.port_a.h_outflow, 0, 0) - valveIncompressible.state_a.T) * ((-3.0) + (valveIncompressible.port_b.m_flow / (-valveIncompressible.m_flow_small)) ^ 2.0) * (valveIncompressible.port_b.m_flow / valveIncompressible.m_flow_small) else 0.5 * (valveIncompressible.state_a.T + Modelica.Media.Water.IF97_Utilities.T_ph(pipe2.port_b.p, valveIncompressible.port_a.h_outflow, 0, 0))) ($RES_BND_346)
(259)     [SCAL] (1) $SEV_26 = valveIncompressible1.state_a.d > 0.0 ($RES_EVT_517)
(260)     [SCAL] (1) valveIncompressible.port_b_T = smooth(1, if $SEV_49 then valveIncompressible.state_b.T else if $SEV_50 then Modelica.Media.Water.IF97_Utilities.T_ph(valveIncompressible.port_b.p, valveIncompressible.port_b.h_outflow, 0, 0) else if $SEV_51 then 0.25 * (Modelica.Media.Water.IF97_Utilities.T_ph(valveIncompressible.port_b.p, valveIncompressible.port_b.h_outflow, 0, 0) - valveIncompressible.state_b.T) * ((-3.0) + (valveIncompressible.port_b.m_flow / valveIncompressible.m_flow_small) ^ 2.0) * (valveIncompressible.port_b.m_flow / valveIncompressible.m_flow_small) + 0.5 * (valveIncompressible.state_b.T + Modelica.Media.Water.IF97_Utilities.T_ph(valveIncompressible.port_b.p, valveIncompressible.port_b.h_outflow, 0, 0)) else 0.5 * (valveIncompressible.state_b.T + Modelica.Media.Water.IF97_Utilities.T_ph(valveIncompressible.port_b.p, valveIncompressible.port_b.h_outflow, 0, 0))) ($RES_BND_347)
(261)     [SCAL] (1) $SEV_27 = valveIncompressible1.dp <= (-valveIncompressible1.dp_turbulent) ($RES_EVT_518)
(262)     [SCAL] (1) valveIncompressible.dp_turbulent = max(valveIncompressible.dp_small, (6.283185307179586e6 * (Modelica.Media.Water.IF97_Utilities.dynamicViscosity(valveIncompressible.state_a.d, valveIncompressible.state_a.T, valveIncompressible.state_a.p, valveIncompressible.state_a.phase) + Modelica.Media.Water.IF97_Utilities.dynamicViscosity(valveIncompressible.state_b.d, valveIncompressible.state_b.T, valveIncompressible.state_b.p, valveIncompressible.state_b.phase)) ^ 2.0) / (valveIncompressible.Av * max(valveIncompressible.relativeFlowCoefficient, 0.001) * (valveIncompressible.state_b.d + valveIncompressible.state_a.d))) ($RES_BND_348)
(263)     [SCAL] (1) $SEV_28 = valveIncompressible1.state_b.d > 0.0 ($RES_EVT_519)
(264)     [SCAL] (1) sink.ports[1].m_flow + valveIncompressible.port_b.m_flow = 0.0 ($RES_SIM_300)
(265)     [SCAL] (1) valveIncompressible1.V_flow = -valveIncompressible1.port_b.m_flow / smooth(1, if $SEV_47 then valveIncompressible1.state_a.d else if $SEV_48 then valveIncompressible1.state_b.d else if $SEV_46 then 0.5 * (valveIncompressible1.state_a.d + valveIncompressible1.state_b.d) - 0.25 * (valveIncompressible1.state_b.d - valveIncompressible1.state_a.d) * ((-3.0) + (valveIncompressible1.port_b.m_flow / (-valveIncompressible1.m_flow_small)) ^ 2.0) * (valveIncompressible1.port_b.m_flow / valveIncompressible1.m_flow_small) else 0.5 * (valveIncompressible1.state_a.d + valveIncompressible1.state_b.d)) ($RES_BND_349)
(266)     [SCAL] (1) pipe1.heatTransfer.heatPorts[1].Q_flow = 0.0 ($RES_SIM_301)
(267)     [ARRY] (2) pipe2.crossAreasFM[:] = {pipe2.crossAreas[1], pipe2.crossAreas[1]} ($RES_SIM_130)
(268)     [ARRY] (1) pipe2.dheightsFM[:] = {0.0} ($RES_SIM_131)
(269)     [ARRY] (1) pipe2.pathLengths[:] = {10.0} ($RES_SIM_132)
(270)     [ARRY] (1) pipe2.Wb_flows = (pipe2.crossAreas * pipe2.vs * (($FUN_6 + pipe2.port_b.p) - ((system.g * {0.0}) / pipe2.mediums.d + 99999.99999999999 * splitter.medium.p_bar))) / ({1.0} * {1.0}) .* {1.0} .* pipe2.nParallel ($RES_SIM_133)
(271)     [ARRY] (1) pipe2.Qb_flows = pipe2.heatTransfer.Q_flows ($RES_SIM_134)
(272)     [ARRY] (1) pipe2.heatTransfer.Q_flows = pipe2.heatTransfer.heatPorts.Q_flow ($RES_SIM_135)
(273)     [ARRY] (1) pipe2.heatTransfer.Ts = pipe2.heatTransfer.heatPorts.T ($RES_SIM_136)
(274)     [ARRY] (1) {0.0} = pipe2.flowModel.Ib_flows - (pipe2.flowModel.Fs_fg + pipe2.flowModel.Fs_p) ($RES_SIM_137)
(275)     [ARRY] (1) pipe2.flowModel.Is = {pipe2.flowModel.m_flows[1] * pipe2.flowModel.pathLengths[1]} ($RES_SIM_138)
(276)     [ARRY] (1) pipe2.flowModel.dps_fg = {(2.0 * (pipe2.flowModel.Fs_fg[1] / pipe2.flowModel.nParallel)) / (pipe2.flowModel.crossAreas[1] + pipe2.flowModel.crossAreas[2])} ($RES_SIM_139)
(277)     [RECD] (5) pipe1.statesFM[1] = pipe1.state_a ($RES_SIM_220)
(278)     [SCAL] (1) pipe1.port_b.h_outflow = pipe1.mediums[1].h ($RES_SIM_223)
(279)     [ARRY] (1) pipe3.mediums.phase = pipe3.mediums.state.phase ($RES_SIM_95)
(280)     [SCAL] (1) pipe1.port_a.h_outflow = pipe1.mediums[1].h ($RES_SIM_224)
(281)     [ARRY] (1) pipe3.mediums.d = pipe3.mediums.state.d ($RES_SIM_96)
(282)     [SCAL] (1) $SEV_29 = valveIncompressible1.state_a.d >= valveIncompressible1.state_b.d ($RES_EVT_520)
(283)     [SCAL] (1) pipe1.port_b.m_flow = -pipe1.m_flows[2] ($RES_SIM_225)
(284)     [SCAL] (1) valveIncompressible1.port_a_T = smooth(1, if $SEV_47 then valveIncompressible1.state_a.T else if $SEV_48 then Modelica.Media.Water.IF97_Utilities.T_ph(pipe3.port_b.p, valveIncompressible1.port_a.h_outflow, 0, 0) else if $SEV_46 then 0.5 * (valveIncompressible1.state_a.T + Modelica.Media.Water.IF97_Utilities.T_ph(pipe3.port_b.p, valveIncompressible1.port_a.h_outflow, 0, 0)) - 0.25 * (Modelica.Media.Water.IF97_Utilities.T_ph(pipe3.port_b.p, valveIncompressible1.port_a.h_outflow, 0, 0) - valveIncompressible1.state_a.T) * ((-3.0) + (valveIncompressible1.port_b.m_flow / (-valveIncompressible1.m_flow_small)) ^ 2.0) * (valveIncompressible1.port_b.m_flow / valveIncompressible1.m_flow_small) else 0.5 * (valveIncompressible1.state_a.T + Modelica.Media.Water.IF97_Utilities.T_ph(pipe3.port_b.p, valveIncompressible1.port_a.h_outflow, 0, 0))) ($RES_BND_350)
(285)     [ARRY] (1) pipe3.mediums.T = pipe3.mediums.state.T ($RES_SIM_97)
(286)     [SCAL] (1) $SEV_30 = valveIncompressible1.relativeFlowCoefficient < valveIncompressible1.minLimiter.uMin ($RES_EVT_521)
(287)     [SCAL] (1) pipe1.port_a.m_flow = pipe1.m_flows[1] ($RES_SIM_226)
(288)     [SCAL] (1) valveIncompressible1.port_b_T = smooth(1, if $SEV_44 then valveIncompressible1.state_b.T else if $SEV_45 then Modelica.Media.Water.IF97_Utilities.T_ph(valveIncompressible1.port_b.p, valveIncompressible1.port_b.h_outflow, 0, 0) else if $SEV_46 then 0.25 * (Modelica.Media.Water.IF97_Utilities.T_ph(valveIncompressible1.port_b.p, valveIncompressible1.port_b.h_outflow, 0, 0) - valveIncompressible1.state_b.T) * ((-3.0) + (valveIncompressible1.port_b.m_flow / valveIncompressible1.m_flow_small) ^ 2.0) * (valveIncompressible1.port_b.m_flow / valveIncompressible1.m_flow_small) + 0.5 * (valveIncompressible1.state_b.T + Modelica.Media.Water.IF97_Utilities.T_ph(valveIncompressible1.port_b.p, valveIncompressible1.port_b.h_outflow, 0, 0)) else 0.5 * (valveIncompressible1.state_b.T + Modelica.Media.Water.IF97_Utilities.T_ph(valveIncompressible1.port_b.p, valveIncompressible1.port_b.h_outflow, 0, 0))) ($RES_BND_351)
(289)     [ARRY] (1) pipe3.mediums.p = pipe3.mediums.state.p ($RES_SIM_98)
(290)     [SCAL] (1) $SEV_31 = valveIncompressible.dp >= valveIncompressible.dp_turbulent ($RES_EVT_522)
(291)     [SCAL] (1) pipe1.H_flows[2] = -$FUN_4 ($RES_SIM_227)
(292)     [SCAL] (1) valveIncompressible1.dp_turbulent = max(valveIncompressible1.dp_small, (6.283185307179586e6 * (Modelica.Media.Water.IF97_Utilities.dynamicViscosity(valveIncompressible1.state_a.d, valveIncompressible1.state_a.T, valveIncompressible1.state_a.p, valveIncompressible1.state_a.phase) + Modelica.Media.Water.IF97_Utilities.dynamicViscosity(valveIncompressible1.state_b.d, valveIncompressible1.state_b.T, valveIncompressible1.state_b.p, valveIncompressible1.state_b.phase)) ^ 2.0) / (valveIncompressible1.Av * max(valveIncompressible1.relativeFlowCoefficient, 0.001) * (valveIncompressible1.state_b.d + valveIncompressible1.state_a.d))) ($RES_BND_352)
(293)     [ARRY] (1) pipe3.mediums.h = pipe3.mediums.state.h ($RES_SIM_99)
(294)     [SCAL] (1) $SEV_32 = valveIncompressible.state_a.d > 0.0 ($RES_EVT_523)
(295)     [SCAL] (1) pipe1.H_flows[1] = $FUN_3 ($RES_SIM_228)
(296)     [SCAL] (1) $SEV_33 = valveIncompressible.dp <= (-valveIncompressible.dp_turbulent) ($RES_EVT_524)
(297)     [SCAL] (1) pipe1.mb_flows[1] = pipe1.m_flows[1] - pipe1.m_flows[2] ($RES_SIM_229)
(298)     [SCAL] (1) $SEV_34 = valveIncompressible.state_b.d > 0.0 ($RES_EVT_525)
(299)     [ARRY] (1) pipe2.fluidVolumes = {10.0 * pipe2.crossAreas[1]} .* pipe2.nParallel ($RES_BND_355)
(300)     [SCAL] (1) $SEV_35 = valveIncompressible.state_a.d >= valveIncompressible.state_b.d ($RES_EVT_526)
(301)     [ARRY] (1) pipe2.mediums.p_bar = {1e-5 * pipe2.mediums[1].p} ($RES_BND_356)
(302)     [SCAL] (1) $SEV_36 = valveIncompressible.relativeFlowCoefficient < valveIncompressible.minLimiter.uMin ($RES_EVT_527)
(303)     [ARRY] (1) pipe2.mediums.T_degC = {(-273.15) + pipe2.mediums[1].T} ($RES_BND_357)
(304)     [FOR-] (2) ($RES_EVT_528)
(304)     [----] for $i1 in 1:2 loop
(304)     [----]   [SCAL] (1) $SEV_37[$i1] = pipe1.flowModel.m_flows[$i1] > 0.0 ($RES_EVT_529)
(304)     [----] end for;
(305)     [ARRY] (2) pipe2.flowModel.vs = pipe2.vsFM ($RES_BND_358)
(306)     [SCAL] (1) valveIncompressible.port_b.p = sink.ports[1].p ($RES_SIM_310)
(307)     [ARRY] (2) pipe2.flowModel.crossAreas = pipe2.crossAreasFM ($RES_BND_359)
(308)     [SCAL] (1) valveIncompressible1.port_b.p = sink.ports[2].p ($RES_SIM_311)
(309)     [SCAL] (1) pipe1.port_a.m_flow + source.ports[1].m_flow = 0.0 ($RES_SIM_312)
(310)     [SCAL] (1) source.ports[1].p = pipe1.port_a.p ($RES_SIM_313)
(311)     [ARRY] (1) pipe2.flowModel.Fs_p = pipe2.flowModel.nParallel * {0.5 * (pipe2.flowModel.crossAreas[1] + pipe2.flowModel.crossAreas[2]) * (pipe2.flowModel.states.phase - pipe2.flowModel.states.phase)} ($RES_SIM_140)
(312)     [ARRY] (1) pipe2.flowModel.Ib_flows = {0.0} ($RES_SIM_141)
(313)     [SCAL] (1) pipe2.flowModel.rhos_act[1] = noEvent(if $SEV_18 then pipe2.flowModel.rhos[1] else pipe2.flowModel.rhos[2]) ($RES_SIM_142)
(314)     [SCAL] (1) pipe2.flowModel.mus_act[1] = noEvent(if $SEV_18 then pipe2.flowModel.mus[1] else pipe2.flowModel.mus[2]) ($RES_SIM_143)
(315)     [ARRY] (1) pipe2.flowModel.m_flows = {homotopy(({$FUN_5} .* pipe2.flowModel.nParallel)[1], (pipe2.flowModel.m_flow_nominal / pipe2.flowModel.dp_nominal * (pipe2.flowModel.dps_fg - (pipe2.flowModel.g * pipe2.flowModel.dheights) .* pipe2.flowModel.rho_nominal))[1])} ($RES_SIM_144)
(316)     [SCAL] (1) pipe1.Hb_flows[1] = pipe1.H_flows[1] - pipe1.H_flows[2] ($RES_SIM_230)
(317)     [ARRY] (3) pipe1.roughnessesFM[:] = {pipe1.roughnesses[1], pipe1.roughnesses[1], pipe1.roughnesses[1]} ($RES_SIM_231)
(318)     [ARRY] (3) pipe1.dimensionsFM[:] = {pipe1.dimensions[1], pipe1.dimensions[1], pipe1.dimensions[1]} ($RES_SIM_232)
(319)     [ARRY] (3) pipe1.crossAreasFM[:] = {pipe1.crossAreas[1], pipe1.crossAreas[1], pipe1.crossAreas[1]} ($RES_SIM_233)
(320)     [ARRY] (2) pipe1.dheightsFM[:] = {0.0, 0.0} ($RES_SIM_234)
(321)     [SCAL] (1) $SEV_38[1] = pipe1.mediums[1].p >= 0.0 ($RES_EVT_530)
(322)     [ARRY] (2) pipe1.pathLengths[:] = {5.0, 5.0} ($RES_SIM_235)
(323)     [ARRY] (2) pipe2.flowModel.dimensions = pipe2.dimensionsFM ($RES_BND_360)
(324)     [ARRY] (1) pipe1.Wb_flows = (pipe1.crossAreas * pipe1.vs * (($FUN_2 + 99999.99999999999 * splitter.medium.p_bar) - ((system.g * {0.0}) / pipe1.mediums.d + pipe1.port_a.p))) / ({1.0} * {1.0}) .* {1.0} .* pipe1.nParallel ($RES_SIM_236)
(325)     [ARRY] (2) pipe2.flowModel.roughnesses = pipe2.roughnessesFM ($RES_BND_361)
(326)     [SCAL] (1) $SEV_40 = (pipe1.mediums[1].h < Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(pipe1.mediums.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(pipe1.mediums.sat.psat)) or pipe1.mediums[1].h > Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(pipe1.mediums.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(pipe1.mediums.sat.psat))) or pipe1.mediums[1].p > 2.2064e7 ($RES_EVT_532)
(327)     [ARRY] (1) pipe1.Qb_flows = pipe1.heatTransfer.Q_flows ($RES_SIM_237)
(328)     [ARRY] (1) pipe2.flowModel.dheights = pipe2.dheightsFM ($RES_BND_362)
(329)     [ARRY] (1) pipe1.heatTransfer.Q_flows = pipe1.heatTransfer.heatPorts.Q_flow ($RES_SIM_238)
(330)     [ARRY] (1) pipe2.flowModel.pathLengths = pipe2.pathLengths ($RES_BND_363)
(331)     [ARRY] (1) pipe1.heatTransfer.Ts = pipe1.heatTransfer.heatPorts.T ($RES_SIM_239)
(332)     [FOR-] (2) ($RES_BND_364)
(332)     [----] for $i1 in 1:2 loop
(332)     [----]   [SCAL] (1) pipe2.flowModel.rhos[$i1] = pipe2.flowModel.states.d ($RES_BND_365)
(332)     [----] end for;
(333)     [SCAL] (1) $SEV_43 = (source.medium.h < Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(source.medium.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(source.medium.sat.psat)) or source.medium.h > Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(source.medium.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(source.medium.sat.psat))) or source.p > 2.2064e7 ($RES_EVT_535)
(334)     [SCAL] (1) $SEV_44 = valveIncompressible1.port_b.m_flow > valveIncompressible1.m_flow_small ($RES_EVT_536)
(335)     [FOR-] (2) ($RES_BND_366)
(335)     [----] for $i1 in 1:2 loop
(335)     [----]   [SCAL] (1) pipe2.flowModel.mus[$i1] = Modelica.Media.Water.IF97_Utilities.dynamicViscosity(pipe2.flowModel.states.d, pipe2.flowModel.states.h, pipe2.flowModel.states.phase, pipe2.flowModel.states.p) ($RES_BND_367)
(335)     [----] end for;
(336)     [SCAL] (1) $SEV_45 = valveIncompressible1.port_b.m_flow < (-valveIncompressible1.m_flow_small) ($RES_EVT_537)
(337)     [SCAL] (1) $SEV_46 = valveIncompressible1.m_flow_small > 0.0 ($RES_EVT_538)
(338)     [ARRY] (1) pipe2.flowModel.pathLengths_internal = pipe2.flowModel.pathLengths ($RES_BND_368)
(339)     [SCAL] (1) $SEV_47 = (-valveIncompressible1.port_b.m_flow) > valveIncompressible1.m_flow_small ($RES_EVT_539)
(340)     [SCAL] (1) pipe2.flowModel.Res_turbulent_internal[1] = pipe2.flowModel.Re_turbulent ($RES_BND_369)
(341)     [ARRY] (1) pipe2.mediums.phase = pipe2.mediums.state.phase ($RES_SIM_150)
(342)     [ARRY] (1) pipe2.mediums.d = pipe2.mediums.state.d ($RES_SIM_151)
(343)     [ARRY] (1) pipe2.mediums.T = pipe2.mediums.state.T ($RES_SIM_152)
(344)     [ARRY] (1) pipe2.mediums.p = pipe2.mediums.state.p ($RES_SIM_153)
(345)     [ARRY] (1) pipe2.mediums.h = pipe2.mediums.state.h ($RES_SIM_154)
(346)     [SCAL] (1) pipe2.mediums[1].u = pipe2.mediums[1].h - pipe2.mediums[1].p / pipe2.mediums[1].d ($RES_SIM_156)
(347)     [ARRY] (1) pipe2.mediums.sat.psat = pipe2.mediums.p ($RES_SIM_157)
(348)     [SCAL] (1) pipe2.mediums[1].sat.Tsat = Modelica.Media.Water.IF97_Utilities.BaseIF97.Basic.tsat(pipe2.mediums[1].p) ($RES_SIM_158)
(349)     [SCAL] (1) pipe2.mediums[1].T = Modelica.Media.Water.IF97_Utilities.T_props_ph(pipe2.mediums[1].p, pipe2.mediums[1].h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(pipe2.mediums[1].p, pipe2.mediums[1].h, pipe2.mediums[1].phase, 0)) ($RES_SIM_159)
(350)     [ARRY] (2) {0.0 for $i1 in 1:2} = pipe1.flowModel.Ib_flows - (pipe1.flowModel.Fs_fg + pipe1.flowModel.Fs_p) ($RES_SIM_240)
(351)     [ARRY] (2) pipe1.flowModel.Is = {pipe1.flowModel.m_flows[i] * pipe1.flowModel.pathLengths[i] for i in 1:2} ($RES_SIM_241)
(352)     [ARRY] (2) pipe1.flowModel.dps_fg = {pipe1.flowModel.Fs_fg[i] / pipe1.flowModel.nParallel * 2.0 / (pipe1.flowModel.crossAreas[i] + pipe1.flowModel.crossAreas[i + 1]) for i in 1:2} ($RES_SIM_242)
(353)     [ARRY] (2) pipe1.flowModel.Fs_p = pipe1.flowModel.nParallel * {0.0 for i in 1:2} ($RES_SIM_243)
(354)     [ARRY] (2) pipe1.flowModel.Ib_flows = {0.0 for $i1 in 1:2} ($RES_SIM_244)
(355)     [SCAL] (1) $SEV_48 = (-valveIncompressible1.port_b.m_flow) < (-valveIncompressible1.m_flow_small) ($RES_EVT_540)
(356)     [FOR-] (2) ($RES_SIM_245)
(356)     [----] for $i1 in 1:2 loop
(356)     [----]   [SCAL] (1) pipe1.flowModel.rhos_act[$i1] = noEvent(if $SEV_37[$i1] then pipe1.flowModel.rhos[$i1] else pipe1.flowModel.rhos[$i1 + 1]) ($RES_SIM_246)
(356)     [----] end for;
(357)     [ARRY] (1) pipe2.flowModel.diameters = 0.5 * (pipe2.flowModel.dimensions[2:2] + pipe2.flowModel.dimensions[1:1]) ($RES_BND_370)
(358)     [SCAL] (1) $SEV_49 = valveIncompressible.port_b.m_flow > valveIncompressible.m_flow_small ($RES_EVT_541)
(359)     [SCAL] (1) $SEV_50 = valveIncompressible.port_b.m_flow < (-valveIncompressible.m_flow_small) ($RES_EVT_542)
(360)     [FOR-] (2) ($RES_SIM_247)
(360)     [----] for $i1 in 1:2 loop
(360)     [----]   [SCAL] (1) pipe1.flowModel.mus_act[$i1] = noEvent(if $SEV_37[$i1] then pipe1.flowModel.mus[$i1] else pipe1.flowModel.mus[$i1 + 1]) ($RES_SIM_248)
(360)     [----] end for;
(361)     [ARRY] (1) pipe2.vs = {(0.5 * (pipe2.m_flows[2] + pipe2.m_flows[1])) / (pipe2.crossAreas[1] * pipe2.mediums[1].d)} / pipe2.nParallel ($RES_BND_372)
(362)     [SCAL] (1) $SEV_51 = valveIncompressible.m_flow_small > 0.0 ($RES_EVT_543)
(363)     [SCAL] (1) $SEV_52 = (-valveIncompressible.port_b.m_flow) > valveIncompressible.m_flow_small ($RES_EVT_544)
(364)     [ARRY] (2) pipe1.flowModel.m_flows = {homotopy(({$FUN_1 for $i1 in 1:2} .* pipe1.flowModel.nParallel)[$i1], (pipe1.flowModel.m_flow_nominal / pipe1.flowModel.dp_nominal * (pipe1.flowModel.dps_fg - pipe1.flowModel.g * pipe1.flowModel.dheights .* pipe1.flowModel.rho_nominal))[$i1]) for $i1 in 1:2} ($RES_SIM_249)
(365)     [ARRY] (1) pipe2.heatTransfer.Ts = {pipe2.heatTransfer.states.h} ($RES_BND_374)
(366)     [SCAL] (1) $SEV_53 = (-valveIncompressible.port_b.m_flow) < (-valveIncompressible.m_flow_small) ($RES_EVT_545)
(367)     [ARRY] (1) pipe2.heatTransfer.vs = pipe2.vs ($RES_BND_375)
(368)     [ARRY] (1) pipe3.fluidVolumes = {10.0 * pipe3.crossAreas[1]} .* pipe3.nParallel ($RES_BND_379)
(369)     [SCAL] (1) pipe2.mediums[1].d = Modelica.Media.Water.IF97_Utilities.rho_props_ph(pipe2.mediums[1].p, pipe2.mediums[1].h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(pipe2.mediums[1].p, pipe2.mediums[1].h, pipe2.mediums[1].phase, 0)) ($RES_SIM_160)
(370)     [SCAL] (1) pipe2.mediums[1].phase = if $SEV_21 then 1 else 2 ($RES_SIM_161)
(371)     [FOR-] (2) ($RES_SIM_163)
(371)     [----] for $i1 in 1:2 loop
(371)     [----]   [SCAL] (1) sink.ports[$i1].p = sink.p ($RES_SIM_164)
(371)     [----] end for;
(372)     [FOR-] (2) ($RES_SIM_165)
(372)     [----] for $i1 in 1:2 loop
(372)     [----]   [SCAL] (1) sink.ports[$i1].h_outflow = sink.medium.h ($RES_SIM_166)
(372)     [----] end for;
(373)     [SCAL] (1) sink.medium.h = Modelica.Media.Water.IF97_Utilities.h_pT(sink.p, sink.T, 0) ($RES_SIM_167)